KR20150041755A - Method for forming ti-containing film by peald using tdmat or tdeat - Google Patents
Method for forming ti-containing film by peald using tdmat or tdeat Download PDFInfo
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- KR20150041755A KR20150041755A KR20140136089A KR20140136089A KR20150041755A KR 20150041755 A KR20150041755 A KR 20150041755A KR 20140136089 A KR20140136089 A KR 20140136089A KR 20140136089 A KR20140136089 A KR 20140136089A KR 20150041755 A KR20150041755 A KR 20150041755A
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- 238000000034 method Methods 0.000 title claims abstract description 73
- 239000010936 titanium Substances 0.000 claims abstract description 50
- 239000000758 substrate Substances 0.000 claims abstract description 24
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- 230000008021 deposition Effects 0.000 claims abstract description 4
- 239000012495 reaction gas Substances 0.000 claims abstract 5
- 239000007789 gas Substances 0.000 claims description 86
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 70
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 49
- 239000000376 reactant Substances 0.000 claims description 41
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 39
- 229910010413 TiO 2 Inorganic materials 0.000 claims description 37
- 229910052799 carbon Inorganic materials 0.000 claims description 37
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 35
- 229910052760 oxygen Inorganic materials 0.000 claims description 29
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 28
- 239000001301 oxygen Substances 0.000 claims description 28
- 239000013078 crystal Substances 0.000 claims description 27
- MNWRORMXBIWXCI-UHFFFAOYSA-N tetrakis(dimethylamido)titanium Chemical compound CN(C)[Ti](N(C)C)(N(C)C)N(C)C MNWRORMXBIWXCI-UHFFFAOYSA-N 0.000 claims description 27
- 229910052757 nitrogen Inorganic materials 0.000 claims description 22
- 229910010282 TiON Inorganic materials 0.000 claims description 19
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 19
- VJDVOZLYDLHLSM-UHFFFAOYSA-N diethylazanide;titanium(4+) Chemical compound [Ti+4].CC[N-]CC.CC[N-]CC.CC[N-]CC.CC[N-]CC VJDVOZLYDLHLSM-UHFFFAOYSA-N 0.000 claims description 19
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 claims description 17
- 238000000137 annealing Methods 0.000 claims description 8
- 238000000231 atomic layer deposition Methods 0.000 claims description 7
- 238000000151 deposition Methods 0.000 claims description 7
- 239000003153 chemical reaction reagent Substances 0.000 claims description 6
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 4
- 229910001882 dioxygen Inorganic materials 0.000 claims description 4
- PWVDYRRUAODGNC-UHFFFAOYSA-N CCN([Ti])CC Chemical compound CCN([Ti])CC PWVDYRRUAODGNC-UHFFFAOYSA-N 0.000 abstract 1
- 125000002147 dimethylamino group Chemical group [H]C([H])([H])N(*)C([H])([H])[H] 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 description 32
- 239000001257 hydrogen Substances 0.000 description 30
- 239000010410 layer Substances 0.000 description 27
- 239000012528 membrane Substances 0.000 description 27
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 26
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 22
- 239000002243 precursor Substances 0.000 description 19
- 229910021529 ammonia Inorganic materials 0.000 description 13
- 238000002441 X-ray diffraction Methods 0.000 description 10
- 125000004429 atom Chemical group 0.000 description 10
- 239000011159 matrix material Substances 0.000 description 10
- 230000008569 process Effects 0.000 description 10
- 238000001228 spectrum Methods 0.000 description 10
- 230000015572 biosynthetic process Effects 0.000 description 8
- 238000001039 wet etching Methods 0.000 description 8
- 230000008901 benefit Effects 0.000 description 7
- 230000002829 reductive effect Effects 0.000 description 7
- 238000001312 dry etching Methods 0.000 description 6
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 5
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- 239000012159 carrier gas Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 239000002356 single layer Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 229910011208 Ti—N Inorganic materials 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000002050 diffraction method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- 238000005240 physical vapour deposition Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- 229910052718 tin Inorganic materials 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 125000001664 diethylamino group Chemical group [H]C([H])([H])C([H])([H])N(*)C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 description 1
- 238000000059 patterning Methods 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- 238000000623 plasma-assisted chemical vapour deposition Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
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- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/02104—Forming layers
- H01L21/02365—Forming inorganic semiconducting materials on a substrate
- H01L21/02612—Formation types
- H01L21/02617—Deposition types
- H01L21/0262—Reduction or decomposition of gaseous compounds, e.g. CVD
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
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- C23C16/45523—Pulsed gas flow or change of composition over time
- C23C16/45525—Atomic layer deposition [ALD]
- C23C16/45527—Atomic layer deposition [ALD] characterized by the ALD cycle, e.g. different flows or temperatures during half-reactions, unusual pulsing sequence, use of precursor mixtures or auxiliary reactants or activations
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
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- C23C16/45523—Pulsed gas flow or change of composition over time
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
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Abstract
Description
본 발명은 일반적으로, 테트라키스(디메틸아미노)티타늄 (TDMAT) 및/또는 테트라키스(디에틸아미노)티타늄 (TDEAT) 을 사용하여 플라즈마 강화 원자 층 증착 (PEALD) 에 의해 Ti 함유 막을 형성하는 방법에 관한 것이다.The present invention generally relates to a method for forming a Ti containing film by plasma enhanced atomic layer deposition (PEALD) using tetrakis (dimethylamino) titanium (TDMAT) and / or tetrakis (diethylamino) titanium .
Ti 계 막들은 스퍼터링 방법, PVD 방법, 및 CVD 방법에 의해 오랫 동안 형성되어 왔고, 예를 들어, 낮은 시트 저항을 갖는 TiN 막들은 구리 확산 차단 막들로서 상업적으로 사용되어왔다. 또한, 최근의 디바이스 노드들의 축소에 따라, SDDP (spacer-defined double patterning) 는 점차적으로 소형화를 위한 기술로서 사용되기 시작했고, TiO 및 TiN 은 SDDP 용 하드 마스크들을 위한 양호한 후보들로 고려된다. SDDP 하드 마스크들을 위하여, 양호한 스텝 커버리지를 갖는 컨포멀 막 (conformal film) 들이 하드 마스크들의 성질의 관점에서 필요하고, 따라서 당업자들은, 일반적으로 양호한 스텝 커버리지를 제공하는 ALD 방법에 의해 형성된 TiO 및 TiN 계 컨포멀 막들을 사용 및 평가했다. 특히, TiN 은 일반적으로 응력을 제어하기 어렵고 그것은 강하게 압축성이 되기 쉽고, 따라서 응력을 제어하는 것은 난제들 중 하나이다. 게다가, 디바이스 노드들의 소형화에 기인하여, 스퍼터링 방법, PVD 방법, 및 CVD 방법과 같은 종래 방법들에 의해 양호한 스텝 커버리지를 갖는 컨포멀 막들을 형성하는 것은 어려웠고, 따라서, 대안의 방법으로서, 양호한 스텝 커버리지 및 낮은 시트 저항을 갖는 막들을 형성하는 방법이 요망된다.Ti based films have been formed for a long time by a sputtering method, a PVD method, and a CVD method. For example, TiN films having low sheet resistance have been used commercially as copper diffusion barrier films. Also, with the recent shrinkage of device nodes, spacer-defined double patterning (SDDP) has gradually begun to be used as a technology for miniaturization, and TiO and TiN are considered good candidates for hard masks for SDDP. For SDDP hard masks, conformal films with good step coverage are needed in terms of the nature of the hard masks, and therefore those skilled in the art will appreciate that TiO2 and TiN < RTI ID = 0.0 > Conformal membranes were used and evaluated. In particular, TiN is generally difficult to control stresses and it is likely to be strongly compressible, and thus controlling stress is one of the challenges. In addition, due to the miniaturization of device nodes, it has been difficult to form conformal films with good step coverage by conventional methods such as sputtering methods, PVD methods, and CVD methods, and therefore, as an alternative method, And a method of forming films having low sheet resistance are desired.
본 발명의 개요Summary of the Invention
본 발명의 일부의 실시형태들에 따르면, 테트라키스(디메틸아미노)티타늄 (TDMAT) 또는 테트라키스(디에틸아미노)티타늄 (TDEAT) 을 플라즈마 강화 원자층 증착 (PEALD) 을 위한 전구체로서 사용함에 있어서, 단순히 반응물 가스를 변경함으로써, TiN, TiCN, TiO, TiON, 및 TiOCN 막들과 같은 다양한 타입의 막이 형성될 수 있고, 또한, 막에 통상적인 각 막의 막 품질이 제어될 수 있다. 일부 실시형태들에서, TDMAT 또는 TDEAT 와 동시에 암모니아가 사용되지 않아서, TDMAT 또는 TDEAT 가 암모니아에 매우 반응성일지라도, 전구체와 그 전구체와 함께 사용된 암모니아 사이의 반응이 회피될 수 있다.According to some embodiments of the present invention, in using tetrakis (dimethylamino) titanium (TDMAT) or tetrakis (diethylamino) titanium (TDEAT) as a precursor for plasma enhanced atomic layer deposition (PEALD) By simply changing the reagent gas, various types of films can be formed, such as TiN, TiCN, TiO, TiON, and TiOCN films, and also the film quality of each film typical of the film can be controlled. In some embodiments, the reaction between the precursor and the ammonia used with the precursor may be avoided, although ammonia is not used at the same time as TDMAT or TDEAT, so that TDMAT or TDEAT is highly reactive with ammonia.
다양한 타입의 막 중에서, TiN 막들 및 열적으로 어닐링된 TiO 막들이 결정질 성분들에 의해 구성될 수도 있다. TiCN 막들은 결정질 및 비정질 성분들의 혼합물에 의해 구성될 수도 있고, TiCN 막들의 탄소 함량이 높으면, 막들은 전체적으로 비정질 성분들에 의해 구성된다. 다른 타입의 막들이 비정질 성분들에 의해 구성된다. TiN 및 TiCN 막들을 형성함에 있어서, 질소 공급 가스가 종종 질화에 사용된다. 하지만, 일부 실시형태들에서, TiN 막들을 형성함에 있어서, 질소 공급 가스인 암모니아가 사용되는 것이 아니라, 수소가 반응물 가스로서 사용되며, 그에 의해 전구체 자체에 포함된 질소를 사용하여 TiN 막들을 형성한다. 일부 실시형태들에서, 수소 가스만이 TiN 막들을 형성하기 위한 반응물 가스로서 사용된다. 일부 실시형태들에서, 질소 가스가 사용될 수도 있지만; 질소 가스가 본질적으로 질소 공급 가스로서 사용되는 것이 아니라, 탄소 농도, 막 응력 및/또는 시트 저항을 제어하는데 사용된다. 따라서, 일부 실시형태들은, TiN 막들이 질소 티타늄 결합들을 갖는 메틸아민 종인 전구체를 사용하여 형성될 수 있고, 수소 흐름, 질소 흐름, 및/또는 RF 전력을 파라미터들로서 다른 막 형성 조건들과 조합함으로써, 막 품질이 효과적으로 제어될 수 있는 것을 특징으로 한다.Among the various types of films, TiN films and thermally annealed TiO films may be constituted by crystalline components. The TiCN films may be composed of a mixture of crystalline and amorphous components, and if the carbon content of the TiCN films is high, the films are generally constituted by amorphous components. Other types of membranes are composed of amorphous components. In forming TiN and TiCN films, a nitrogen feed gas is often used for nitridation. However, in some embodiments, in forming TiN films, ammonia, which is a nitrogen feed gas, is not used but hydrogen is used as a reactant gas, thereby forming TiN films using nitrogen contained in the precursor itself . In some embodiments, only hydrogen gas is used as the reactant gas to form TiN films. In some embodiments, nitrogen gas may be used; Nitrogen gas is not used essentially as a nitrogen feed gas, but is used to control carbon concentration, film stress, and / or sheet resistance. Thus, some embodiments can be formed using TiN films using precursors that are methylamine species with nitrogen-titanium bonds, and by combining hydrogen flow, nitrogen flow, and / or RF power with other film- And the film quality can be effectively controlled.
관련 기술에 수반된 문제 및 해법들에 대한 임의의 논의는 오로지 본 발명을 위한 맥락을 제공하는 목적을 위해서만 포함되고, 그 논의의 일부 또는 전부가 본 발명이 이루어진 당시에 알려져 있었다라는 것을 인정하는 것으로 받아들여져서는 안된다. Any discussion of the problems and solutions associated with the related art is only included for purposes of providing a context for the present invention and acknowledged that some or all of the discussion was known at the time the invention was made It should not be imported.
본 발명의 양태들 및 관련 기술에 비해 달성되는 이점들을 요약하는 목적으로, 본 발명의 특정 목적들 및 이점들이 본 개시에서 설명된다. 물론, 모든 그러한 목적들 또는 이점들이 반드시 본 발명의 임의의 특정 실시형태에 따라 달성되는 것은 아닐 수도 있다는 것이 이해되야 한다. 따라서, 예를 들어, 당업자는, 본 발명이 여기에 교시되거나 또는 시사될 수도 있는 바처럼 반드시 다른 목적들 또는 이점들을 달성하는 것은 아닌 여기에 교시된 바처럼 하나의 이점 또는 이점들의 군을 달성하거나 또는 최적화하는 방식으로 구체화되거나 또는 수행될 수도 있다는 것을 인식할 것이다.For purposes of summarizing the aspects of the invention and the advantages achieved relative to the related art, certain objects and advantages of the invention are set forth in the present disclosure. Of course, it should be understood that not all such objects or advantages may be achieved in accordance with any particular embodiment of the invention. Thus, for example, those skilled in the art will readily appreciate that the present invention is not limited to achieving other objects or advantages, such as may be taught or suggested herein, but rather achieves one or a group of benefits or advantages as taught herein Or may be embodied or performed in a manner that is optimized.
본 발명의 추가 양태들, 특징들 및 이점들은 다음의 상세한 설명으로부터 분명해질 것이다. Further aspects, features and advantages of the present invention will become apparent from the following detailed description.
본 발명의 이들 및 다른 특징들이 이제 본 발명을 제한하는 것이 아닌 본 발명을 예시하도록 의도된 바람직한 실시형태들의 도면들을 참조하여 설명될 것이다. 그 도면들은 예시적인 목적들로 대폭 단순화되고 반드시 스케일대로인 것은 아니다.
도 1은 본 발명의 실시형태에서 사용가능한, 유전체 막을 성막하기 위한 PEALD 장치의 개략도이다.
도 2(a)는 테트라키스(디메틸아미노)티타늄 (TDMAT) 의 화학식을 나타낸다.
도 2(b)는 본 발명의 실시형태에 따라 수소 플라즈마를 이용하여 형성된 결정질 TiN 막의 매트릭스 구조를 나타내는 개략적인 예시이고, 여기서 N-C 결합들이 끊어지고, 탄소들이 매트릭스에 들어가지 않는다.
도 2(c)는 수소 플라즈마를 사용하지 않고서 형성된 비정질 TiCN 막의 매트릭스 구조를 나타내는 개략적인 예시이고, 여기서 N-C 결합들이 유지되고, 탄소들이 매트릭스내에 들어가고 결정질 구조의 형성을 방해한다.
도 3은, 본 발명의 실시형태에 따른, 막이 아나타제 타입 결정들을 형성한다는 것을 나타내는, 어닐링된 막의 X-선 회절 분석의 결과를 나타낸다.
도 4는 본 발명의 실시형태에 따른 컨포멀 TiCN 막의 단면도의 투과 전자 현미경 (TEM) 사진이다.
도 5는 본 발명의 실시형태에 따른 반응물 가스로서 암모니아를 사용하여 유전체 막을 성막하기 위한 PEALD 방법의 프로세스 단계들을 나타낸다.
도 6은 본 발명의 일부 실시형태에 따른 유전체 막을 성막하기 위한 PEALD 방법의 프로세스 단계들을 나타낸다.
도 7은 본 발명의 실시형태에 따른 TiN 및 TiO 막들 또는 TiCN 및 TiO 막들로 이루어지는 TiON 또는 TiOCN 막의 라미네이트 구조를 나타내는 개략도이다.
도 8은 본 발명의 일부 실시형태들에 따른 TiN 막, TiO 막, 및 TiON 막의 건식 식각 레이트들을 나타내는 그래프이다.
도 9는 본 발명의 일부 실시형태들에 따른 TiN 막, TiO 막, 및 TiON 막의 습식 식각 레이트들을 나타내는 그래프이다.
도 10은 본 발명의 일부 실시형태들에 따른 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들을 나타낸다.
도 11은 본 발명의 일부 실시형태들에 따른 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들을 나타낸다.
도 12는 본 발명의 일부 실시형태들에 따른 TiN/TiCN 막의 결정질에 관한 막 응력의 범위를 나타내는 그래프이다.
도 13은 본 발명의 일부 실시형태들에 따른 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들을 나타낸다.
도 14는: 본 발명의 일부 실시형태들에 따른 (a) TiCN 막 (탄소 함량: 6%) 의 X-선 회절 분석의 결과, 그리고 (b) TiCN 막 (탄소 함량: 16%) 의 X-선 회절 분석의 결과를 나타낸다.
도 15는: 본 발명의 일부 실시형태들에 따른 (a) TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들, 그리고 (b) TiCN 막들의 X-선 회절 분석의 결과들을 나타낸다.
도 16은: 본 발명의 일부 실시형태들에 따른 (a) TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들, 그리고 (b) TiCN 막들의 X-선 회절 (XRD) 분석의 결과들을 나타낸다.
도 17 은 본 발명의 일부 실시형태들에 따른, 막 응력과 수소 흐름 사이의 관계를 나타내는 그래프와, 막 응력과 RF 전력 사이의 관계를 나타내는 그래프를 도시한다.These and other aspects of the present invention will now be described with reference to the drawings of preferred embodiments, which are intended to illustrate the invention without limiting the invention. The figures are greatly simplified for illustrative purposes and are not necessarily to scale.
1 is a schematic view of a PEALD device for forming a dielectric film usable in an embodiment of the present invention.
Figure 2 (a) shows the chemical formula of tetrakis (dimethylamino) titanium (TDMAT).
Fig. 2 (b) is a schematic illustration showing a matrix structure of a crystalline TiN film formed using a hydrogen plasma according to an embodiment of the present invention, where the NC bonds are broken, and the carbons do not enter the matrix.
Figure 2 (c) is a schematic illustration showing a matrix structure of an amorphous TiCN film formed without the use of a hydrogen plasma, where the NC bonds are retained and the carbons enter the matrix and interfere with the formation of a crystalline structure.
Figure 3 shows the results of an X-ray diffraction analysis of an annealed film, showing that the film forms anatase type crystals, in accordance with an embodiment of the present invention.
4 is a transmission electron microscope (TEM) photograph of a cross-sectional view of a conformal TiCN film according to an embodiment of the present invention.
Figure 5 depicts the process steps of the PEALD method for depositing a dielectric film using ammonia as a reactant gas in accordance with an embodiment of the present invention.
Figure 6 depicts the process steps of the PEALD method for depositing a dielectric film in accordance with some embodiments of the present invention.
7 is a schematic view showing a laminate structure of a TiON or TiOCN film composed of TiN and TiO films or TiCN and TiO films according to an embodiment of the present invention.
8 is a graph showing dry etch rates of a TiN film, a TiO film, and a TiON film in accordance with some embodiments of the present invention.
9 is a graph showing wet etch rates of a TiN film, a
Figure 10 shows Fourier Transform Infrared (FT-IR) spectra of TiCN films according to some embodiments of the present invention.
Figure 11 shows Fourier Transform Infrared (FT-IR) spectra of TiCN films according to some embodiments of the present invention.
Figure 12 is a graph showing the range of film stresses related to the crystallinity of a TiN / TiCN film in accordance with some embodiments of the present invention.
Figure 13 shows Fourier Transform Infrared (FT-IR) spectra of TiCN films according to some embodiments of the present invention.
Figure 14 shows the results of X-ray diffraction analysis of (a) a TiCN film (carbon content: 6%) according to some embodiments of the present invention and (b) Ray diffraction analysis.
Figure 15 shows the results of (a) Fourier transform infrared (FT-IR) spectra of TiCN films and (b) X-ray diffraction analysis of TiCN films according to some embodiments of the present invention.
Figure 16 shows the results of (a) Fourier transform infrared (FT-IR) spectra of TiCN films and (b) X-ray diffraction (XRD) analysis of TiCN films according to some embodiments of the present invention.
Figure 17 shows a graph showing the relationship between membrane stress and hydrogen flow and a graph showing the relationship between membrane stress and RF power, in accordance with some embodiments of the present invention.
본 개시에서, “가스” 는 증기화된 고체 및/또는 액체를 포함할 수도 있고 단일 가스 또는 가스들의 혼합물에 의해 구성될 수도 있다. 마찬가지로, 관사 "a" 또는 "an" 는 하나의 종을 지칭하거나 또는 다수의 종들을 포함하는 속 (genus) 을 지칭한다. 본 개시에서, 전구체 가스 및 반응물 가스 등의 프로세스 가스는 샤워헤드를 통해 반응 챔버에 도입되고 활성 가스 및 비활성 가스로 구성되거나, 본질적으로 이루어지거나, 또는 이루어질 수도 있다. 즉, 본 개시에서, "전구체 가스" 는 희가스 등의 캐리어 가스와 도입될 수도 있고, 마찬가지로 "반응물 가스" 는 희가스 등의 캐리어 가스와 도입될 수도 있다. 대안적으로, 전구체 또는 반응물 가스는 활성 가스로 이루어질 수도 있다. 희가스는 퍼지 가스로서 샤워헤드를 통해 간헐적으로 또는 연속적으로 도입될 수 있다. 프로세스 가스외의 가스, 즉 샤워헤드를 통과하지 않고서 도입된 가스는, 예를 들어 ,반응 공간을 실링하는데 사용될 수도 있고, 이는 희가스와 같은 시일 가스를 포함한다. 일부 실시형태들에서, "막" 은 실질적으로 핀홀들 없이 두께 방향에 수직한 방향으로 연속적으로 연장되어 전체 타겟 또는 관련 표면 (concerned surface) 을 커버하는 층, 또는 간단히 타겟 또는 관련 표면을 커버하는 층을 지칭한다. 일부 실시형태들에서, "층" 은, 표면 상에 형성된 특정 두께를 갖는 구조물 또는 막의 동의어를 지칭한다. 막 또는 층은, 특정 특성들을 갖는 별개 (discrete) 단일 막 또는 층, 또는 다수의 막들 또는 층들에 의해 구성될 수도 있고, 인접하는 막들 또는 층들 사이의 경계 (boundary) 는 명확 (clear) 하거나 또는 그렇지 않을 수도 있고, 물리적, 화학적 및/또는 임의의 다른 특성들, 형성 프로세스들 또는 시퀀스, 및/또는 인접하는 막들 또는 층들의 기능들 또는 목적들에 기초하여 확립될 수도 있다. 또한, 본 개시에서, 변수의 임의의 2개 수들은 변수의 작업가능한 범위를 구성할 수 있는데, 그 작업가능한 범위는 일상적인 작업 (routine work) 에 기초하여 결정될 수 있기 때문이고, 나타낸 임의의 범위들은 종점 (endpoint) 들을 포함하거나 또는 제외할 수도 있다. 또한, 표시된 변수들의 임의의 값들은 ("약" 으로 표시되든지 또는 그렇지 않든지에 상관 없이) 정확한 값들 또는 근사 값들을 지칭할 수도 있고 등가물 (equivalent) 들을 포함할 수도 있고, 일부의 실시형태들에서는, 평균, 중간 (median), 대표, 다수 (majority) 등을 지칭할 수도 있다.In the present disclosure, " gas " may comprise vaporized solids and / or liquid and may be constituted by a single gas or a mixture of gases. Similarly, the articles "a" or "an" refer to a species or to a genus comprising a plurality of species. In the present disclosure, the process gas, such as precursor gas and reactant gas, is introduced into the reaction chamber through the showerhead and may consist, consist essentially of, or consist of an active gas and an inert gas. That is, in the present disclosure, the "precursor gas" may be introduced with a carrier gas such as rare gas, and similarly, the "reactant gas" may be introduced with a carrier gas such as rare gas. Alternatively, the precursor or reagent gas may consist of an active gas. The rare gas may be introduced intermittently or continuously through the showerhead as purge gas. A gas other than the process gas, that is, the gas introduced without passing through the showerhead, may be used, for example, to seal the reaction space, which includes a seal gas such as rare gas. In some embodiments, a "film" is a layer that extends continuously in a direction perpendicular to the direction of thickness without substantially pinholes to form a layer covering the entire target or an associated surface, or simply a layer covering the target or associated surface Quot; In some embodiments, a "layer" refers to a structure or film synonym having a specific thickness formed on a surface. The film or layer may be composed of a discrete single film or layer with a specific property or multiple films or layers and the boundary between adjacent films or layers may be clear or otherwise And may be established based on physical, chemical and / or any other characteristics, forming processes or sequences, and / or functions or purposes of adjacent layers or layers. Also, in this disclosure, any two numbers of variables can constitute a workable range of a variable, since its operable range can be determined based on routine work, May include or exclude endpoints. In addition, any values of the indicated variables (whether indicated as "about" or not) may refer to exact or approximate values and may include equivalents, and in some embodiments , Mean, median, representative, majority, and the like.
본 개시에서 조건들 및/또는 구조들이 명시되지 않는 경우에, 당업자는, 일상적인 실험의 문제로서, 본 개시를 고려하여, 그러한 조건들 및/또는 구조들을 손쉽게 제공할 수 있다.Where conditions and / or structures are not specified in the present disclosure, those skilled in the art can readily provide such conditions and / or structures in view of this disclosure, as a matter of routine experimentation.
모든 개시된 실시형태들에서, 실시형태에 사용된 임의의 요소는 그와 동등한 임의의 요소에 의해 치환될 수 있고, 의도된 목적들을 위해 여기에서 명시적으로, 필요적으로, 또는 내재적으로 개시된 것들을 포함한다. 또한, 본 발명은 장치 및 방법들에 동일하게 적용될 수 있다.In any of the disclosed embodiments, any element used in the embodiments may be replaced by any element equivalent thereto and includes those explicitly, necessarily, or implicitly disclosed herein for intended purposes . Furthermore, the present invention is equally applicable to apparatus and methods.
본 개시에서, 임의의 정의된 의미들은 일부 실시형태들에서 보통 및 관습적인 의미들을 반드시 제외하는 것은 아니다.In this disclosure, any defined meanings are not necessarily excluded from the ordinary and customary meanings in some embodiments.
일부 실시형태들에서, 테트라키스(디메틸아미노)티타늄 (TDMAT) 또는 테트라키스(디에틸아미노)티타늄 (TDEAT) 을 사용하여 플라즈마 강화 원자층 증착 (PEALD) 에 의해 기판 상에 Ti 함유 막을 형성하는 방법은 : (i) 기판이 배치되는 반응 공간에 펄스로 TDMAT 및/또는 TDEAT 를 도입하는 단계; (ii) 반응 공간에 NH3 무함유 반응물 가스를 연속적으로 도입하는 단계; (iii) 반응 공간에 펄스로 RF 전력을 인가하는 단계로서, TDMAT 및/또는 TDEAT 의 펄스 그리고 RF 전력의 펄스는 오버랩되지 않는, 상기 인가하는 단계; 및 (iv) 기판 상에 Ti 함유 막을 성막하기 위하여 (i) 내지 (iii) 단계들을 반복하는 단계를 포함한다.In some embodiments, a method of forming a Ti-containing film on a substrate by plasma enhanced atomic layer deposition (PEALD) using tetrakis (dimethylamino) titanium (TDMAT) or tetrakis (diethylamino) (I) introducing TDMAT and / or TDEAT into the reaction space in which the substrate is placed in a pulse; (ii) continuously introducing an NH 3 -containing reactant gas into the reaction space; (iii) applying RF power in pulses to the reaction space, wherein pulses of TDMAT and / or TDEAT and pulses of RF power do not overlap; And (iv) repeating steps (i) to (iii) to form a Ti-containing film on the substrate.
일부 실시형태들에서, TDMAT 및 TDEAT 는 이들에 동등한 유도체들을 포함할 수도 있고, 여기에서 메틸 기들 및 에틸 기들은 교환가능하게 사용될 수 있다.In some embodiments, TDMAT and TDEAT may include equivalent derivatives to these, where methyl groups and ethyl groups may be used interchangeably.
위에서, "연속적으로" 는, 진공 파괴 없이, 타임라인으로서 중단 없이, 처리 조건들을 변경함이 없이, 또는 일부의 실시형태들에서는 그 직후에를 지칭한다.Above, "continuously" refers to without vacuum break, without interruption as a timeline, without changing processing conditions, or in some embodiments immediately thereafter.
일부 실시형태들에서, NH3 무함유 반응물 가스는 H2 및/또는 N2이다. 일부 실시형태들에서, NH3 무함유 반응물 가스는, 질소, 산소 및 탄소 중 어느 것도 함유하지 않는다. 일부 실시형태들에서, NH3 무함유 반응물 가스는 H2 및 희가스 (예를 들어, He, Ar) 로 이루어지고, 이에 의해 (iv) 단계에서 Ti 함유 막으로서 TiN 결정질 막을 성막한다. 대안적으로, 일부 실시형태들에서, NH3 무함유 반응물 가스는 H2, N2, 및 희가스 (예를 들어, He, Ar) 로 이루어지고, 이에 의해 (iv) 단계에서 Ti 함유 막으로서 TiCN 비정질 막을 성막한다. 대안적으로, 일부 실시형태들에서, NH3 무함유 반응물 가스는 산소를 포함하고, 이에 의해 (iv) 단계에서 Ti 함유 막으로서 TiO 막을 형성한다. 일부 실시형태들에서, 그 방법은, (iv) 단계에서 Ti 함유 막으로서 아나타제 결정을 갖는 TiO 막을 형성하기 위하여, (iv) 단계 후에 산소의 분위기에서 기판 상에 Ti 함유 막을 어닐링하는 단계를 더 포함하고, 여기서 비정질 TiO 는 아나타제 결정들로 변화된다. 아나타제 결정을 갖는 TiO 막은 광촉매 활성을 나타낸다. 어닐링 후에, TiO 막의 표면은 친수성을 획득하고, 이는 TiO 광촉매에 고유한 초친수성이다.In some embodiments, the NH 3 -containing reactant gas is H 2 and / or N 2 . In some embodiments, the NH 3 -containing reactant gas does not contain any of nitrogen, oxygen, and carbon. In some embodiments, the NH 3 -containing reactant gas comprises H 2 and rare gases (eg, He, Ar), thereby forming a TiN crystalline film as the Ti containing film in step (iv). Alternatively, in some embodiments, the NH 3 -containing reactant gas comprises H 2 , N 2 , and rare gases (eg, He, Ar), thereby forming TiCN An amorphous film is formed. Alternatively, in some embodiments, the NH 3 -containing reactant gas comprises oxygen, thereby forming a
일부 실시형태들에서, NH3 무함유 반응물 가스는 산소를 함유하지 않는 반응물 가스 그리고 산소를 함유하는 반응물 가스로 구성되고, (iv) 단계에서, (i) 내지 (iii) 단계들이 반복될 때, NH3 무함유 산소 무함유 반응물 가스 및 NH3 무함유 산소 함유 가스가 설정된 인터벌에서 교번하여 사용된다. 예를 들어, NH3 무함유 산소 무함유 반응물 가스는 질소 가스 없이 수소 가스이고, NH3 무함유 산소 함유 가스는 산소 가스이고, 이에 의해 설정된 인터벌에서 교번하여 성막된 TiO 막들과 TiN 막들로 이루어지는 TiON 막을 형성한다. 대안적으로, 일부 실시형태들에서, NH3 무함유 산소 무함유 반응물 가스는 수소 가스 및 질소 가스이고, NH3 무함유 산소 함유 가스는 산소 가스이고, 이에 의해 설정된 인터벌에서 교번하여 성막된 TiO 막들과 TiCN 막들로 이루어지는 TiOCN 막을 형성한다. 도 7은 본 발명의 실시형태에 따른 기판 (71) 상에 형성된 TiN 및 TiCN 막들 (72, 74, 76, 78) 및 TiO 막들 (73, 75, 77) 로 이루어지는 TiON 또는 TiOCN 막 (79) 의 라미네이트 구조를 나타내는 개략도이다. 본 실시형태에서, 먼저, TiN 또는 TiCN 서브 층을 형성하는 사이클은 5 내지 100번 수행되어 기판 (71) 상에 TiN 또는 TiCN 막 (72) 을 형성하고, 다음으로, TiO 서브 층을 형성하는 사이클은 한번 수행되어 TiN 또는 TiCN 막 (72) 상부에 TiO 막 (73) 을 형성한다. 마찬가지로, TiN 또는 TiCN 막 (74), TiO 막 (75), TiN 또는 TiCN 막 (76), TiO 막 (77), 및 TiN 또는 TiCN 막 (78) 이 이 순서대로 성막되어 라미네이트 (79) 를 형성한다. 일부 실시형태들에서, TiO 막을 형성하는 사이클의 수는 TiN 또는 TiCN 막을 형성하는 사이클들의 수보다 현저히 더 적다, 즉 TiO 막의 두께는 TiN 또는 TiCN 막의 두께보다 현저히 더 작다. 일부 실시형태들에서, 라미네이트들 (각 라미네이트는, 하나 이상의 TiN/TiCN 서브 층들로 구성될 수도 있는 단일 TiN/TiCN 막, 및 하나 이상의 TiO 서브 층들로 구성될 수도 있는 단일 TiO 막에 의해 구성됨) 의 수는 약 3 내지 200, 통상적으로 5 내지 100이다. 일부 실시형태들에서, 하나의 라미네이트에서 TiO 막을 형성하는 사이클들의 수 대 TiN/TiCN 막을 형성하는 사이클들의 수의 비는 1:1 내지 1:200, 통상적으로 1:3 내지 1:100, 보다 통상적으로는 1:5 내지 1:25 일 수도 있다. 또한, 도 5는 반응물 가스로서 암모니아를 사용하여 유전체 막을 성막하기 위한 PEALD 방법의 프로세스 단계들을 나타낸다. 도 6은 본 발명의 일부 실시형태에 따른 유전체 막을 성막하기 위한 PEALD 방법의 프로세스 단계들을 나타낸다. 도 6에 예시된 실시형태들에서, 암모니아가 반응물 가스로서 사용되지 않았기 때문에, 반응물 가스 (질소, 수소, 및/또는 산소) 가 연속적으로 공급될 수 있고, 또한 전구체 피드의 펄스와 RF 전력 인가의 펄스 사이의 퍼지 가스로서 기능할 수 있다. 위에서, 반응물 가스는 캐리어 가스로서 사용되는 희가스 (미도시) 와 함께 공급된다. 대조적으로, 도 5에서, 암모니아가 반응물 가스로서 사용되었기 때문에, 반응물 가스는 전구체 피드의 펄스와는 상이한 펄스로 공급되야 하고, 이는 서로 오버랩되지 않아야 하며, 더 복잡한 제어 시스템을 필요로 한다.In some embodiments, the NH 3 -containing reactant gas is comprised of a reactant gas that does not contain oxygen and a reactant gas that contains oxygen, and in step (iv), when steps (i) to (iii) The NH 3 -free oxygen-free reagent gas and the NH 3 -free oxygen-containing gas are alternately used at the set intervals. For example, the NH 3 -free oxygen-free reactant gas is hydrogen gas without nitrogen gas, and the NH 3 -free oxygen-containing gas is oxygen gas, whereby
본 개시에서, TiN, TiON, TiCN, TiOCN, TiO 막들, 및 다른 Ti 함유 막은, 매트릭스들이 실질적으로 또는 대부분 위에 나타낸 원소들로 구성되지만, 불순물, 비실질적인 원소들 이를테면 수소, 그리고 비실질적인 양의 재료 원소들을 제외하지 않은 막들을 지칭하거나, 또는 주로 그 나타낸 원소들에 의해 특성화되는 막들, 그 나타낸 원소들에 의해 표현되는 막들, 또는 당업자가 그렇게 인식하는 막들을 지칭한다.In the present disclosure, the TiN, TiON, TiCN, TiOCN, TiO2 films, and other Ti containing films are formed from a mixture of impurities, non-substantial elements such as hydrogen, Refers to films that do not exclude elements, or to films that are characterized primarily by the elements they represent, to films that are represented by the elements shown, or to those skilled in the art.
일부 실시형태들에서, TiN 막은 아래의 표 1에 나타낸 조건들하에서 형성될 수 있다. ALD 는 자기 제한 흡착 반응 프로세스이므로, 성막되는 전구체 분자들의 양은 반응 표면 사이트들의 수에 의해 결정되고, 포화 후의 전구체 노출과 관계 없고, 전구체의 공급은, 그에 의해 반응 표면 사이트들이 사이클마다 포화되도록 한다.In some embodiments, a TiN film can be formed under the conditions shown in Table 1 below. Since ALD is a self-limiting adsorption reaction process, the amount of precursor molecules deposited is determined by the number of reactive surface sites, independent of the precursor exposure after saturation, and the supply of precursors thereby causing the reaction surface sites to saturate per cycle.
일부 실시형태들에서, TiCN 막은 아래의 표 2에 나타낸 조건들하에서 형성될 수 있다.In some embodiments, a TiCN film can be formed under the conditions shown in Table 2 below.
일부 실시형태들에서, TiON 막은 아래의 표 4에 나타낸 조건들하에서 형성될 수 있다.In some embodiments, the TiON film may be formed under the conditions shown in Table 4 below.
일부 실시형태들에서, TiOCN 막은 아래의 표 5에 나타낸 조건들하에서 형성될 수 있다.In some embodiments, a TiOCN film can be formed under the conditions shown in Table 5 below.
일부 실시형태들에서, Ti 함유 막의 두께는, 막의 조성, 막의 의도된 용도 등에 따라, 약 0.3nm 내지 약 60nm, 통상적으로 약 0.06nm 내지 약 300nm 의 범위에 있을 수도 있다.In some embodiments, the thickness of the Ti containing film may range from about 0.3 nm to about 60 nm, typically from about 0.06 nm to about 300 nm, depending on the composition of the film, the intended use of the film, and the like.
일부 실시형태들에서, TiO 막은 아나타제 결정들을 형성하기 위하여 아래 표 6에 나타낸 조건들하에서 어닐링을 받는다.In some embodiments, the
어닐링을 수행하는 것에 의해, 아나타제 타입 결정들, 루틸 타입 (rutile-type) 결정들, 또는 브루카이트 (brookite-type) 타입 결정들이, 어닐링 온도에 따라, 형성될 수 있다. 예를 들어, 막이 약 600℃에서 어닐링될 때, 아나타제 타입 결정들이 형성된다. 어닐링을 위해, 산화 분위기를 제공하는 한, 임의의 가스가 사용될 수 있다.By performing the annealing, anatase type crystals, rutile-type crystals, or brookite-type type crystals can be formed, depending on the annealing temperature. For example, when the film is annealed at about 600 < 0 > C, anatase type crystals are formed. For annealing, any gas may be used as long as it provides an oxidizing atmosphere.
일부 실시형태들에서, Ti 함유 막은 막 응력이 -2,500 MPa 내지 800 MPa 이다. 도 12는 본 발명의 일부 실시형태들에 따른 TiN/TiCN 막의 결정질에 관한 막 응력의 범위를 나타내는 그래프이다. 도 12에 나타낸 바처럼, 막이 매우 결정질일 때, 즉 낮은 탄소 함량을 가질 때, 막은 높은 압축 응력을 갖고, 막이 전체적으로 비정질일 때, 막은 압축 응력이 약 -400 MPa이다. 막의 탄소 함량이 약 4% 와 약 9% 사이일 때, 막은 막에 포함된 결정 구조의 타입들에 따라, 인장 응력을 가질 수 있다. 즉, 막 응력은 2개 이상의 타입의 결정 구조에 관련되는 것으로 보이고, 결정 구조들의 비율에 따라, 막은 높은 막 응력 내지 낮은 막 응력을 나타낸다. 하지만, 막의 탄소 함량이 약 4% 보다 적거나 또는 약 9% 보다 많을 때, 인장 응력을 나타내는 결정 구조들을 형성하기 어려운 것으로 보인다. 일부 실시형태들에서, 막의 탄소 함량이 약 6% 일 때, 막은 최고 인장 응력, 약 800 MPa 를 갖는다. 막의 최저 압축 응력은 약 -2,500 MPa 이하일 수도 있고, 막의 탄소 함량이 검출가능하지 않을 때 (ND), 막은 최저 압축 응력을 나타낼 수도 있다. 막의 탄소 함량이 약 6% 보다 많을 때, 막은 최저 압축 응력을 나타내지 않을 수도 있다.In some embodiments, the Ti containing film has a film stress of -2,500 MPa to 800 MPa. Figure 12 is a graph showing the range of film stresses related to the crystallinity of a TiN / TiCN film in accordance with some embodiments of the present invention. As shown in FIG. 12, when the film is very crystalline, that is, when it has a low carbon content, the film has a high compressive stress, and when the film is amorphous as a whole, the film has a compressive stress of about -400 MPa. When the carbon content of the film is between about 4% and about 9%, the film may have tensile stress, depending on the types of crystal structure contained in the film. That is, the film stress appears to be related to two or more types of crystal structures, and depending on the proportion of the crystal structures, the film exhibits high to low film stresses. However, when the carbon content of the film is less than about 4% or greater than about 9%, it appears that it is difficult to form crystalline structures exhibiting tensile stress. In some embodiments, when the carbon content of the film is about 6%, the film has a peak tensile stress, about 800 MPa. The minimum compressive stress of the film may be about -2,500 MPa or less, and when the carbon content of the film is not detectable (ND), the film may exhibit the lowest compressive stress. When the carbon content of the film is greater than about 6%, the film may not exhibit the lowest compressive stress.
막의 결정질은 막 형성 파라미터들을 변경하는 것에 의해 조정될 수 있다. 몇몇 실시형태들에서, 그 방법은 : (a) (ii) 단계에서 반응물 가스로서 사용된 H2 의 참조 유량 (reference flow rate), (iii) 단계에서 사용된 참조 RF 전력, 및 (i) 내지 (iii) 전체에 걸친 참조 성막 온도를 포함하는 성막 조건들하에서 (i) 내지 (iv) 단계들에 의해 성막되는 TiN 결정질 막의 막 응력보다 더 큰, Ti 함유 막을 위한 타겟 막 응력을 설정하는 단계; 및 (b) (ii) 단계에서 반응물 가스로서 사용되는 H2 의 유량, (iii) 단계에서 사용되는 RF 전력, 및 (i) 내지 (iii) 단계 전체에 걸친 성막 온도를 설정하는 단계로서, H2 의 유량, RF 전력 및 성막 온도 중 하나 이상만이 막 응력을 변경하기 위한 제어 파라미터로서 사용되고, H2 의 참조 유량, 참조 RF 전력, 및 참조 성막 온도와는 상이한, 상기 설정하는 단계, 다음으로 Ti 함유 막을 성막하기 위해 (i) 내지 (iv) 단계들을 수행하는 단계를 더 포함한다. 일반적으로, RF 전력이 더 높아질 수록, 막 응력이 더 낮아지고, 온도가 더 높아질 수록, 막 응력이 더 높아지며, 수소 함량이 더 높아질 수록, 막 응력이 더 높아진다. 제어 파라미터들의 참조 값들을 참조하여, 제어 파라미터들을 조정함으로써, Ti 함유 막이 인장 막 응력을 갖도록 구성될 수 있다. 예를 들어, 인장 막 응력을 제공하기 위하여, H2 의 유량은 TiN 결정질 막에 사용되는 H2 의 참조 유량보다 더 낮게 설정될 수 있거나, RF 전력은 TiN 결정질 막에 사용되는 참조 RF 전력보다 더 낮게 설정될 수 있거나, 및/또는 성막 온도는 TiN 결정질 막에 사용되는 참조 성막 온도보다 더 높게 설정될 수 있다. 일부 실시형태들에서, Ti 함유 막이 약 4% 내지 약 9% 탄소를 함유할 때, 막은 인장 막 응력을 갖는다.The crystalline quality of the film can be adjusted by changing film formation parameters. In some embodiments, the method comprises: (a) determining a reference flow rate of H 2 used as the reactant gas in step (ii), a reference RF power used in step (iii), and (i) (iii) setting a target film stress for the Ti-containing film that is greater than the film stress of the TiN crystalline film deposited by the steps (i) to (iv) under film-forming conditions comprising the reference film-forming temperature throughout; And (b) setting a film forming temperature throughout the steps (i) to (iii), wherein the flow rate of H 2 used as the reactant gas in step (ii), the RF power used in step (iii) 2 is used as a control parameter for changing the film stress and only one of at least one of the flow rate, the RF power and the film forming temperature is different from the reference flow rate of H 2 , the reference RF power, and the reference film forming temperature, (I) to (iv) in order to form a film containing a silicon-containing film. In general, the higher the RF power, the lower the membrane stress, the higher the temperature, the higher the membrane stress, the higher the hydrogen content, the higher the membrane stress. By referring to the reference values of the control parameters and adjusting the control parameters, the Ti containing film can be configured to have tensile film stress. For example, in order to provide a tensile film stress, the flow rate of H 2 is may be set lower than the reference flow rate of the H 2 being used for the TiN crystalline film, the RF power is more than the reference RF power used for TiN crystalline film And / or the film formation temperature may be set to be higher than the reference film formation temperature used in the TiN crystalline film. In some embodiments, when the Ti containing film contains about 4% to about 9% carbon, the film has tensile film stress.
막 응력은 막에서 결합 상태에 따라 달라진다. 일부 실시형태들에서, Ti 함유 막은 푸리에 변환 적외 분광 (FT-IR) 그래프에서 2,000 cm-1 및 1,400 cm-1 에서 피크들을 나타낸다. 일반적으로 2,000 cm-1 에서의 피크는 인장 응력을 나타내는 반면, 1,400 cm-1 에서의 피크는 압축 응력을 나타낸다. 이들 응력들의 합이 막의 응력을 나타낸다. 2,000 cm-1 및 1,400 cm-1 에서 피크가 없으면, 막은 강한 압축 응력을 나타내며, 이는 막이 TiN 결정들에 의해 구성됨을 나타낸다. 반응물 가스로서 사용된 수소 가스의 흐름이 증가될 때, 먼저, 1,400 cm-1에서의 피크가 사라지고, 막은 인장 응력을 갖는 막이 된다. 이 상태에서, RF 전력이 증가될 때, 2,000 cm-1에서의 피크가 사라지고, 이는 막의 결정질이 증가하고 막은 강한 압축 응력을 갖는 막이 됨을 나타낸다. 따라서, 2개 파라미터들 (수소 가스 흐름 및 RF 전력) 을 조정함으로써, FT-IR 그래프에서 피크들이 조절될 수 있다; 즉 막 응력이 제어될 수 있다. 어떤 결합이 각 피크에 대응하는지는 알려져 있지 않지만, 2,000 cm-1 및 1,400 cm-1 에서의 피크들 중 어느 하나가 감소될 때, 막에서 탄소 함량이 감소되기 때문에 그 피크들은 탄소에 관련되는 것으로 예상된다. 일부 실시형태들에서, FT-IR 그래프에서 1,400 cm-1 에서의 피크의 높이에 기초하여, 수소 흐름과 막 응력 사이의 관계가 결정될 수 있다. 수소 흐름 및 RF 전력을 조작함으로써 1,400 cm-1 에서의 피크가 2,000 cm-1 에서의 피크보다 더 용이하게 사라질 수 있다. 일부 실시형태들에서, 2,000 cm-1에서의 피크는 막 형성을 위한 온도에 의해 제어될 수 있다. 온도가 높을 때, 2,000 cm-1에서의 피크가 높아진다.The film stress depends on the bonding state in the film. In some embodiments, the Ti containing film exhibits peaks at 2,000 cm -1 and 1,400 cm -1 in a Fourier transform infrared spectroscopy (FT-IR) graph. Generally, peaks at 2,000 cm -1 exhibit tensile stresses, while peaks at 1,400 cm -1 exhibit compressive stresses. The sum of these stresses represents the stress of the film. Without peaks at 2,000 cm -1 and 1,400 cm -1 , the film exhibits strong compressive stresses, indicating that the film is constituted by TiN crystals. When the flow of the hydrogen gas used as the reactant gas is increased, first, the peak at 1,400 cm -1 disappears, and the film becomes a film having a tensile stress. In this state, when the RF power is increased, the peak at 2,000 cm <" 1 > disappears indicating that the crystalline quality of the film increases and the film becomes a film with strong compressive stress. Thus, by adjusting the two parameters (hydrogen gas flow and RF power), the peaks in the FT-IR graph can be adjusted; That is, the film stress can be controlled. It is not known which bond corresponds to each peak, but when one of the peaks at 2,000 cm -1 and 1,400 cm -1 is reduced, the peaks are related to carbon because the carbon content in the film is reduced It is expected. In some embodiments, based on the height of the peak at 1400 cm < -1 > in the FT-IR graph, the relationship between hydrogen flow and membrane stress can be determined. The peak at 1,400 cm -1 by manipulating the hydrogen flow, and RF power can be lost more readily than the peak at 2,000 cm -1. In some embodiments, the peak at 2,000 cm -1 may be controlled by the temperature for film formation. When the temperature is high, the peak at 2,000 cm -1 becomes high.
일부 실시형태들에서, 반응물 가스로서 수소를 증가하게 도입함으로써, 1,400 cm-1 에서의 피크가 낮아지고, 2,000 cm-1 에서의 피크만이 유지되고, 이에 의해 결과적인 막을 인장성으로 만든다. 이 상황에서, RF 전력을 증가시킴으로써, 2,000 cm-1 에서의 피크가 또한 사라지고, 이에 의해 결과적인 막을 압축성으로 만들고, 그 막은 TiN 결정들에 의해 구성된다. 수소 가스 흐름을 사용하지 않고서 RF 전력이 증가될 때, 1,400 cm-1 에서의 피크는 더 높아지고, 막 응력은 매우 압축성이 된다. 일부 실시형태들에서, 1,400 cm-1 에서의 피크는 다수의 결합들에 대응한다, 즉 압축 응력 및 인장 응력을 나타내는 다수의 피크들이 집합적으로 1,400 cm-1에서의 피크를 구성하고, 수소 가스 흐름이 증가될 때, 먼저 인장 응력을 나타내는 피크가 사라지고, 다음으로 압축 응력을 나타내는 피크가 사라지며, 이로써, 1,400 cm-1에서의 피크가 존재하지 않게 하고 인장 응력을 나타내는 2,000 cm-1 에서의 피크만을 남긴다. 결과적으로, 인장 응력을 갖는 막이 획득된다. 일부 실시형태들에서, RF 전력을 증가시키는 것은, RF 전력 인가의 지속시간을 늘리는 것과 대등하고, 그것들은 교환가능하게 사용될 수 있다.In some embodiments, by increasing the hydrogen as the reactant gas, the peak at 1400 cm <" 1 > is lowered and only the peak at 2000 cm < -1 > is maintained, thereby rendering the resulting film tensile. In this situation, by increasing the RF power, the peak at 2,000 cm <" 1 > also disappeared, thereby making the resulting film compressible, and the film constituted by TiN crystals. When RF power is increased without using a hydrogen gas flow, the peak at 1,400 cm <" 1 > is higher and the membrane stress becomes very compressive. In some embodiments, the peak at 1,400 cm -1 corresponds to the number of coupling, that is configured for a plurality of peaks at 1,400 cm -1 peak to collectively represent the compression stress and tensile stress, and hydrogen gas when the flow is increased, the first peak represents the tensile stress disappears, the peaks representing the following compression stress to fall off, and thereby, a peak at 1,400 cm -1 no longer exists, and at 2,000 cm -1 indicates a tensile stress Leaving only the peak. As a result, a film having tensile stress is obtained. In some embodiments, increasing the RF power is equivalent to increasing the duration of the RF power application, and they can be used interchangeably.
TDMAT 및 TDEAT의 구조적으로 중요한 피쳐는, 티타늄 상의 Ti-C 및 Ti-H 와 같은 결합들이 있는 것이 아니라, Ti의 모든 4개 핸드 (hand) 들이 Ti-N 결합이라는 것이다. 도 2(a)는 테트라키스(디메틸아미노)티타늄 (TDMAT) 의 화학식을 나타낸다. 이 피쳐에 기인하여, 분자 구조에 포함된 질소들은 효율적으로 막에 포함될 수 있고, 디메틸아민의 형태로 존재하는 탄소들이 용이하게 수소 플라즈마에 의해 제거될 수 있고, 이에 의해 불순물인 탄소를 제거하고 TiN의 결정화를 증진시킨다. 도 2(b)는 본 발명의 실시형태에 따라 수소 플라즈마를 이용하여 형성된 결정질 TiN 막의 매트릭스 구조를 나타내는 개략적인 예시이고, 여기서 N-C 결합들은 끊어지고, 탄소들이 매트릭스내에 들어가지 않는다. 수소 플라즈마에 의한 탄소들의 감소 (reduction) 는 막의 매트릭스 구조를 결정질로 만들고, 매트릭스 구조를 형성하기 위한 질소들이, 반응물 가스로부터가 아니라, 전구체로부터 제공된다. 도 2(c) 는 수소 플라즈마를 사용하지 않고서 형성된 비정질 TiCN 막의 매트릭스 구조를 나타내는 개략적인 예시이고, 여기서 N-C 결합들이 유지되고, 탄소들이 매트릭스내에 들어가고 결정질 구조의 형성을 방해한다. 다른 한편, 수소 플라즈마의 효과를 약화시키고 반응물 가스로서 질소를 사용함으로써, 탄소들은 막에 존재할 수 있고, 이에 의해 막에서 불순물인 탄소를 남기고 따라서 TiCN 에 의해 구성되는 비정질 막을 형성한다.A structurally important feature of TDMAT and TDEAT is not that there are bonds such as Ti-C and Ti-H on titanium, but all four hands of Ti are Ti-N bonds. Figure 2 (a) shows the chemical formula of tetrakis (dimethylamino) titanium (TDMAT). Due to this feature, the nitrogen contained in the molecular structure can be efficiently included in the film, and the carbons present in the form of dimethylamine can be easily removed by the hydrogen plasma, thereby removing the impurity carbon and forming TiN Lt; / RTI > FIG. 2 (b) is a schematic illustration showing a matrix structure of a crystalline TiN film formed using a hydrogen plasma according to an embodiment of the present invention, wherein the N-C bonds are broken and the carbons do not enter the matrix. The reduction of carbons by the hydrogen plasma makes the matrix structure of the film crystalline and the nitrogen for forming the matrix structure is provided from the precursor, not from the reactant gas. Figure 2 (c) is a schematic illustration showing a matrix structure of an amorphous TiCN film formed without the use of a hydrogen plasma, where the N-C bonds are retained and the carbons enter the matrix and interfere with the formation of a crystalline structure. On the other hand, by weakening the effect of the hydrogen plasma and using nitrogen as the reactant gas, the carbons can be present in the film, thereby leaving an impurity carbon in the film and thus forming an amorphous film constituted by TiCN.
또한, TDMAT 및/또는 TDEAT의 사용과 조합하여, 기판의 표면 상에 흡착된 재료가 처리되는 표면 플라즈마 처리 방법인 PEALD에 의해, 가스 상 (gas phase) 에서 Ti 와 디메틸아민 등의 해리된 리간드들의 재결합에 기인하여 Ti-C 및 Ti-H 결합들을 형성하는 것에 의해 막 품질을 열화시킬 위험성이 기상 반응 방법인 PECVD 와 비교하여 감소될 수 있고, 분자 구조에서 Ti-N 결합들을 자르지 않고서 탄소들이 효율적으로 제거될 수 있다. 상기한 바는 전구체로서 TDMAT 및 TDEAT 의 우월한 특징들이고, 다양한 타입의 막의 성막이 보다 용이해지는 이유이다.It is also possible, in combination with the use of TDMAT and / or TDEAT, for the removal of dissociated ligands, such as Ti and dimethylamine, in the gas phase, by means of PEALD, a surface plasma treatment process in which the adsorbed material is treated on the surface of the substrate. The risk of deteriorating the film quality by forming Ti-C and Ti-H bonds due to recombination can be reduced as compared with the gas phase reaction PECVD, and the carbon can be efficiently removed without cutting Ti-N bonds in the molecular structure As shown in FIG. These are the superior features of TDMAT and TDEAT as precursors and are the reason why the deposition of various types of films is easier.
또한, Ti의 특징으로서, 그것은 산소에 타이트하게 결합될 수 있고, 따라서, Ti 의 산화는 매우 용이하고, 이에 의해 TiO 막을 용이하게 형성한다. 하지만, Ti 와 산소 사이의 타이트한 결합은 탄소 및 질소 등의 다른 원소들의 제거에 기여하고, 따라서, 산소가 TiO 막을 형성하는데 사용될 때, 탄소 및 질소는 산소에 의해 제거되고 막 내에 존재하지 않는다. 따라서, 일부 실시형태들에서, 산소 그리고 질소 및/또는 탄소를 막에서 동시에 남길 때, 즉, TiON 또는 TiOCN 막을 형성할 때, 그것은, TiO 막들 및 TiN 또는 TiCN 막들이 교번하여 라미네이트되는 라미네이션 방법을 사용하는 것에 의해 형성될 수 있다.Further, as a characteristic of Ti, it can be tightly bound to oxygen, and therefore oxidation of Ti is very easy, thereby easily forming a TiO film. However, the tight bond between Ti and oxygen contributes to the removal of other elements such as carbon and nitrogen, and thus, when oxygen is used to form the
일반적으로, TiN의 결정이 전도성일 때, 그리고 TiN의 결정질이 향상될 때, 시트 저항은 낮아진다. 탄소 또는 산소가 막에 포함될 때, 결정질이 열화되고, 그 구조를 비정질로 만든다. 일부 실시형태들에서, 수소 가스 흐름 및 RF 전력을 제어함으로써, 막 응력 및 탄소 농도가 제어될 수 있고, 그에 의해 막의 결정질을 제어하고 시트 저항을 제어한다. 탄소 농도와 막 응력 사이에 관찰되는 강한 상관이 없지만, 탄소 농도가 극히 낮고 결정질이 높을 때, 막은 압축성으로 특성화된다. 이것은, 탄소 농도의 감소에 기인하여 결정질이 향상되고, 그에 의해 막을 압축성으로 만들기 때문일 수도 있다.Generally, when the crystal of TiN is conductive and when the crystalline of TiN is improved, the sheet resistance is lowered. When carbon or oxygen is included in the film, the crystalline is deteriorated and makes its structure amorphous. In some embodiments, by controlling hydrogen gas flow and RF power, the film stress and carbon concentration can be controlled, thereby controlling the crystalline quality of the film and controlling the sheet resistance. There is no strong correlation observed between the carbon concentration and the film stress, but when the carbon concentration is extremely low and the crystalline is high, the film is characterized by compressibility. This may be because the crystallinity is improved due to the decrease of the carbon concentration, thereby making the film compressible.
막 응력을 제어함에 있어서, 인장 응력을 갖는 막을 획득하기 위하여, 수소 공급 및 RF 전력을 조합하여 제어하는 것이 극히 중요하다. 인장 응력을 갖는 막을 형성하기 위해 설정된 것과 비교하여 수소 흐름이 너무 낮거나 RF 전력이 너무 높을 때, 막 응력은 압축 응력으로 변화하고, 따라서, 수소 흐름 및 RF 전력 양자 모두를 제어하는 것이 매우 중요하다.In controlling membrane stress, it is extremely important to control the hydrogen supply and RF power in combination in order to obtain a membrane with tensile stress. When the hydrogen flow is too low or the RF power is too high as compared to that set to form a film with tensile stress, the film stress will change to compressive stress and therefore it is very important to control both hydrogen flow and RF power .
TDMAT 는 암모니아와 동시에 공급될 수 없기 때문에, 암모니아가 막을 성막하는데 사용될 때, 전구체를 공급한 후에, 전구체로부터 암모니아로 가스를 전환시키는 단계가 필요하다. 하지만, 일부 실시형태들에서, 암모니아가 사용되지 않고, 따라서, 전구체를 공급한 후에 전환 단계는 필요하지 않고, 그에 의해 막 성장 레이트를 향상시킨다.Since TDMAT can not be supplied simultaneously with ammonia, when ammonia is used to form a film, it is necessary to convert the gas from the precursor to ammonia after supplying the precursor. However, in some embodiments, ammonia is not used, and therefore, no conversion step is required after supplying the precursor, thereby improving the film growth rate.
TiON 막들을 평가하는 동안에, NF3 에 의한 건조 식각 레이트 및 불화 수소에 의한 습식 식각 레이트가, 교번하여 라미네이트된 TiO 층들과 TiN 층들 사이의 경계에서 변화되는 것이 발견되었다. 즉, 라미네이트가 TiO 층들과 TiN 층들 사이에 경계를 가질 때, TiO 또는 TiN 단일 층과 비교하여, 라미네이트의 NF3 에 의한 건식 식각에 대한 저항이 높고, 라미네이트의 불화 수소에 의한 습식 식각 레이트에 대한 저항이 저하된다. 위의 상관은 TiO 층들과 TiN 층들 사이의 경계의 수가 증가할 때 향상된다. 즉, 경계의 수가 더 높아질 때, 건식 식각에 대한 저항이 더 높아지고 습식 식각에 대한 저항이 더 낮아진다.During the evaluation of the TiON films, it has been found that the dry etch rate by NF 3 and the wet etch rate by hydrogen fluoride alternate at the interface between the
일부 실시형태들에서, 막의 스텝 커버리지는 약 90% 내지 약 105%, 통상적으로 약 95% 이상이다.In some embodiments, the step coverage of the film is from about 90% to about 105%, typically about 95% or more.
그 실시형태들은 바람직한 실시형태들을 참조하여 설명될 것이다. 하지만, 본 발명은 그 바람직한 실시형태들에 한정되지 않는다.The embodiments will be described with reference to the preferred embodiments. However, the present invention is not limited to the preferred embodiments thereof.
도 1은, 바람직하게는 이하의 시퀀스들을 수행하도록 프로그램된 제어들과 함께, 본 발명의 일부 실시형태들에서 사용가능한, PEALD 장치의 개략도이다. 동 도에서, 반응 챔버 (3) 의 내부 (11) 에서 서로 대향하고 평행한 한 쌍의 도전성 평판 전극들 (4, 2) 을 제공하고, HRF 전력 (13.56 MHz 또는 27 MHz) (5) 및 5MHz 이하의 LRF 전력 (400 kHz~500 kHz) (50) 을 일측에 인가하고, 타측에 대해 전기 접지 (12) 하는 것에 의해, 플라즈마가 전극들 사이에서 여기된다. 온도 조절기가 하부 스테이지 (2) (하부 전극) 에 제공되고, 그 위에 놓여진 기판 (1) 의 온도는 주어진 온도로 일정하게 유지된다. 상부 전극 (4) 은 또한 샤워 플레이트의 역할을 하고, 반응 가스 및 희가스가 가스 흐름 제어기 (23), 펄스 흐름 제어 밸브 (31) 및 샤워 플레이트를 통해 반응 챔버 (3) 내에 도입된다. 추가적으로, 반응 챔버 (3) 에서, 배기 파이프 (6) 가 제공되고, 이를 통해 반응 챔버 (3) 의 내부 (11) 에 있는 가스가 배기된다. 추가적으로, 반응 챔버에는 반응 챔버 (3) 의 내부 (11) 로 시일 가스를 도입하기 위하여 시일 가스 흐름 제어기 (24) 가 제공된다 (반응 챔버의 내부에서 반응 구역 및 이송 구역을 분리시키기 위한 분리 플레이트가 동 도로부터 생략되어 있다).Figure 1 is a schematic diagram of a PEALD device, which may be used in some embodiments of the invention, preferably with controls programmed to perform the following sequences. In the figure, a pair of conductive
당업자는, 그 장치가, 본원의 다른 곳에 기재된 성막 및 반응기 세정 프로세스들로 하여금 수행되게 하도록 프로그램되거나 또는 다른 방법으로 구성된 하나 이상의 제어기(들) (미도시) 를 포함한다는 것을 인식할 것이다. 제어기(들) 은 다양한 전력 소스들, 가열 시스템들, 펌프들, 로보틱스 및 가스 흐름 제어기들 또는 반응기의 밸브들과 연통되는데, 이는 당업자에 의해 인식될 것이다.Those skilled in the art will recognize that the apparatus includes one or more controller (s) (not shown) that are programmed or otherwise configured to cause the deposition and reactor cleaning processes described elsewhere herein to be performed. The controller (s) are in communication with the various power sources, heating systems, pumps, robotics and gas flow controllers or valves of the reactor, which will be appreciated by those skilled in the art.
실시예Example
예 1 내지 6Examples 1 to 6
Ti 함유 막들이, 도 6에 예시된 시퀀스 및 도 1에 예시된 장치를 사용하여 이하의 표 7 및 8에 나타낸 조건들하에서 패턴들 (종횡비: 2:1) 을 갖는 기판들 상에 성막되었다.Ti containing films were deposited on substrates having patterns (aspect ratio: 2: 1) under the conditions shown in Tables 7 and 8 below using the sequence illustrated in FIG. 6 and the apparatus illustrated in FIG.
이렇게 획득된 막들이 평가되었고, 그 결과들은 표 9에 나타나 있다.The membranes thus obtained were evaluated, and the results are shown in Table 9.
표 9에 나타낸 바처럼, TiN 막들이, 질소 흐름 없이 상대적으로 높은 흐름의 수소를 사용하여 (예 5), 그리고 상대적으로 높은 RF 전력으로 상대적으로 높은 흐름의 수소를 사용하여 (예 4) 형성되었다. 수소 흐름에 상대적으로 질소 흐름이 증가되었을 때, 막에서 탄소 함량이 증가되었고, 그에 의해 TiCN 막들 (예 1 내지 3) 을 형성한다. 예 1 내지 5에서, 각 막의 스텝 커버리지는 95% 이상이었고, 막 응력은 -3,800 MPa 과 +620 MPa 사이에서 변화되었고, 또한, 각 막은 습식 식각에 대해 높은 저항을 나타냈다. 예 6에서, 높은 품질의 TiO 막이 형성되었다. 도 4는, 예 3에서 형성된 컨포멀 TiCN 막의 단면도의 투과 전자 현미경 (TEM) 사진이다.As shown in Table 9, TiN films were formed (Example 4) using a relatively high flow of hydrogen without nitrogen flow (Example 5) and a relatively high flow of hydrogen with a relatively high RF power (Example 4) . When the nitrogen flow is increased relative to the hydrogen flow, the carbon content in the film is increased, thereby forming TiCN films (Examples 1 to 3). In Examples 1 to 5, the step coverage of each film was greater than 95%, the film stress varied between -3,800 MPa and +620 MPa, and each film exhibited a high resistance to wet etching. In Example 6, a
예 7-10Example 7-10
Ti 함유 막들이, 도 6에 예시된 시퀀스 및 도 1에 예시된 장치를 사용하여 표 8 및 이하의 표 10에 나타낸 조건들하에서 패턴들 (종횡비: 2:1) 을 갖는 기판들 상에 성막되었다.Ti containing films were deposited on substrates having patterns (aspect ratio: 2: 1) under the conditions shown in Table 8 and Table 10 below using the sequence illustrated in FIG. 6 and the apparatus illustrated in FIG. 1 .
이렇게 획득된 막들이 평가되었고, 그 결과들은 표 11 내지 13에 나타나 있다.The membranes thus obtained were evaluated, and the results are shown in Tables 11-13.
예 7 내지 9 에서, 경향으로서, RF 전력이 더 낮을 때, 그리고 온도가 더 높을 때, 탄소 함량이 더 높아졌다. 표 11 내지 13에 나타낸 바처럼, RF 전력을 감소시키고 온도를 증가시킴으로써, 막의 탄소 함량이 감소되었고, 막 응력이 압축성이 되었다 (예 7 내지 9). 예 7 내지 9에서, 각 막의 스텝 커버리지는 약 100% 였고, 막 응력은 약 -4,500 MPa 과 +2,000 MPa 사이에서 변화되었고, 또한, 각 막은 습식 식각에 대해 높은 저항을 나타냈다. 예 10에서, 높은 품질의 TiO 막이 형성되었고, 이는 RF 전력 및 온도의 변화에 의해 현저히 영향받지 않았다.In Examples 7 to 9, as a trend, the carbon content was higher when the RF power was lower and when the temperature was higher. By reducing the RF power and increasing the temperature, as shown in Tables 11-13, the carbon content of the membrane was reduced and the membrane stress became compressible (Examples 7 to 9). In Examples 7 to 9, the step coverage of each film was about 100%, the film stress was varied between about -4,500 MPa and +2,000 MPa, and each film exhibited a high resistance to wet etching. In Example 10, a
예 11-16Example 11-16
라미네이트들에 의해 구성된 Ti 함유 막들이, 도 6에 예시된 시퀀스 및 도 1에 예시된 장치를 사용하여 이하의 표 14 및 15에 나타낸 조건들하에서 패턴들 (종횡비: 2:1) 을 갖는 기판들 상에 성막되었다.The Ti-containing films constituted by the laminates were laminated to the substrates having patterns (aspect ratio: 2: 1) under the conditions shown in Tables 14 and 15 below using the sequence illustrated in Fig. 6 and the apparatus illustrated in Fig. It was settled on.
예 16에서, 각 TiCN 층이 예 1에 있는 것과 같은 조건하에서 형성되었다.In Example 16, each TiCN layer was formed under the same conditions as in Example 1.
이렇게 획득된 막들이 평가되었고, 그 결과들은 표 16에 나타나 있다.The membranes thus obtained were evaluated, and the results are shown in Table 16.
표 16에 나타낸 바처럼, 예 13-16 에서 라미네이트들의 습식 및 건식 식각 레이트 성질들은 예 11 및 12에 있는 2개의 베이스 막들의 그러한 것들간의 범위내에 속하는 것이 아니라 그들의 양자 모두와는 상이했다. TiN 막과 TiO 막 사이의 경계의 수가 증가될 때, 건식 식각 레이트가 감소되는 반면에, 습식 식각 레이트는 증가되었다 (예 13-15).As shown in Table 16, the wet and dry etch rate properties of the laminates in Examples 13-16 were not within the range between those of the two base films in Examples 11 and 12, but were different from both of them. As the number of boundaries between the TiN film and the
예 17-19Example 17-19
막들은 예 11, 12, 및 14 에서와 동일한 조건들하에서 형성되었고, 건식 식각 레이트 및 습식 식각 레이트가 각 막에 대해 측정되었다. 도 8은 예 18에서 형성된 TiN 막, 예 17에서 형성된 TiO 막, 그리고 예 19에서 형성된 TiON 막의 건식 식각 레이트들을 나타내는 그래프이다. TiON 막의 건식 식각 레이트는 TiN 막의 그것 및 TiO 막의 그것보다 두드러지게 낮았다. 도 9는 예 18에서 형성된 TiN 막, 예 17에서 형성된 TiO 막, 그리고 예 19에서 형성된 TiON 막의 습식 식각 레이트들을 나타내는 그래프이다. TiON 막의 습식 식각 레이트는 TiN 막의 그것 및 TiO 막의 그것보다 두드러지게 더 높았다.The films were formed under the same conditions as in Examples 11, 12, and 14, and the dry etch rate and wet etch rate were measured for each film. 8 is a graph showing the dry etch rates of the TiN film formed in Example 18, the TiO film formed in Example 17, and the TiON film formed in Example 19; The dry etch rate of the TiON film was significantly lower than that of the TiN film and that of the TiO film. 9 is a graph showing the wet etch rates of the TiN film formed in Example 18, the TiO film formed in Example 17, and the TiON film formed in Example 19; The wet etch rate of the TiON film was significantly higher than that of the TiN film and that of the TiO film.
예 20Example 20
막 형성 프로세스 후에, 막이 약 2시간 동안 약 600℃ 에서 어닐링된 것을 제외하고는, 예 6에서와 동일한 조건하에서 형성되었다. 도 3은, 막이 아나타제 타입 결정들을 형성한다는 것을 나타내는, 어닐링된 막의 X-선 회절 분석의 결과를 나타낸다.After the film forming process, the film was formed under the same conditions as in Example 6, except that the film was annealed at about 600 캜 for about 2 hours. Figure 3 shows the results of an X-ray diffraction analysis of an annealed film, indicating that the film forms anatase type crystals.
예 21-32Example 21-32
Ti 함유 막들이, 도 6에 예시된 시퀀스 및 도 1에 예시된 장치를 사용하여 표 8 및 이하의 표 17에 나타낸 조건들하에서 패턴들 (종횡비: 2:1) 을 갖는 기판들 상에 성막되었다.Ti containing films were deposited on substrates having patterns (aspect ratio: 2: 1) under the conditions shown in Table 8 and Table 17 below using the sequence illustrated in FIG. 6 and the apparatus illustrated in FIG. 1 .
이렇게 획득된 막들이 평가되었고, 그 결과들은 표 18에 나타나 있다.The membranes thus obtained were evaluated, and the results are shown in Table 18.
도 10은 예 21 내지 25에서 형성된 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들을 나타내고, 여기서, 예 21 은 참조예 (“POR”, process of record) 이다. 막 응력은 막에서 결합 상태에 따라 달라졌다. 일반적으로 2,000 cm-1 에서의 피크는 인장 응력을 나타내는 반면, 1,400 cm-1 에서의 피크는 압축 응력을 나타낸다. 이들 응력들의 합이 막의 응력을 나타낸다. 반응물 가스로서 사용된 수소 가스의 흐름이 예 21 내지 23에서 감소되었을 때, 1,400 cm-1에서의 피크는 증가되었고, 막은 압축성이 되었다. 예 21에서, RF 전력이 예 24에서 증가되었을 때, 2,000 cm-1 에서의 피크는 감소되었고, 이는 막의 결정질이 증가되었고, 막이 매우 압축성이 되었음을 나타낸다.10 shows the Fourier Transform Infrared (FT-IR) spectra of the TiCN films formed in Examples 21 to 25, wherein Example 21 is a reference ("POR", process of record). The film stresses varied depending on the bonding state in the film. Generally, peaks at 2,000 cm -1 exhibit tensile stresses, while peaks at 1,400 cm -1 exhibit compressive stresses. The sum of these stresses represents the stress of the film. When the flow of hydrogen gas used as the reactant gas was reduced in Examples 21 to 23, the peak at 1,400 cm <" 1 > was increased and the membrane became compressive. In Example 21, when the RF power was increased in Example 24, the peak at 2,000 cm <" 1 > decreased, indicating that the crystalline quality of the film was increased and the film was very compressive.
도 11은 예 26 내지 29에서 형성된 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들을 나타낸다. 온도가 예 26 내지 29에서 더 높았을 때, 2,000 cm-1에서의 피크가 더 높았다. 2,000 cm-1에서의 피크는 막 형성을 위한 온도에 의해 제어될 수 있다.11 shows Fourier Transform Infrared (FT-IR) spectra of TiCN films formed in Examples 26-29. When the temperature was higher in Examples 26 to 29, the peak at 2,000 cm -1 was higher. The peak at 2,000 cm -1 may be controlled by the temperature for film formation.
도 13은 예 30 내지 32에서 형성된 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들을 나타낸다. RF 전력이 예 30 내지 32에서 수소 가스 흐름을 사용하지 않고서 증가되었을 때, 1,400 cm-1에서의 피크는 더 높아졌고, 2,000 cm-1에서의 피크는 더 낮아졌고, 막 응력이 매우 압축성이 되었다.13 shows Fourier Transform Infrared (FT-IR) spectra of TiCN films formed in Examples 30-32. When the RF power was increased without using a hydrogen gas flow in Examples 30 to 32, the peak at 1,400 cm -1 became higher, the peak at 2,000 cm -1 became lower, and the membrane stress became very compressive .
도 14는 : (a) 예 21에서 획득된 TiCN 막 (탄소 함량: 6%) 의 X-선 회절 분석의 결과, 그리고 (b) 예 23에서 획득된 TiCN 막 (탄소 함량: 16%) 의 X-선 회절 분석의 결과를 나타낸다. 도 14에서 (a) 에 나타낸 바처럼, 낮은 탄소 함량 (6%) 을 갖는 막은 결정질 (예 21) 인 반면에, 도 14에서 (b) 에 나타낸 바처럼, 높은 탄소 함량 (16%) 을 갖는 막은 비정질이었다 (예 23). 막을 구성하는 결정들은, 실질적으로 NaCl 과 동일한 fcc (면심 입방) 구조를 갖는 오스보나이트 TiN 이었다. 막은 다수의 결정들을 포함하지만, 그것들은 주로 (111) 면에서 성장했다.Fig. 14 shows the results of X-ray diffraction analysis of (a) the TiCN film (carbon content: 6%) obtained in Example 21 and (b) the X of the TiCN film (carbon content: 16% Ray diffraction analysis. As shown in Fig. 14 (a), a film having a low carbon content (6%) is crystalline (Example 21), while a film having a high carbon content (16% The membrane was amorphous (Example 23). The crystals constituting the film were os- bonite TiN having a fcc (face-centered cubic) structure substantially the same as NaCl. The film contains a large number of crystals, but they have grown mainly on the (111) plane.
도 15는 : (a) 예 21 내지 23에서 형성된 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들, 및 (b) 예 21 내지 23에서 형성된 TiCN 막들의 X-선 회절 (XRD) 분석의 결과들을 나타낸다. 도 15에 있는 (a) 및 (b) 에 나타낸 바처럼, 1,400 cm-1에서의 피크가 감소되었을 때, XRD 에서 (111) 의 피크는 증가되었고, 이는 1,400 cm-1 에서의 피크가 (111) 결정면 상의 원자 배열과 연관되었다는 것을 나타낸다.Figure 15 shows the results of X-ray diffraction (XRD) analysis of (a) Fourier transform infrared (FT-IR) spectra of TiCN films formed in Examples 21-23 and (b) TiCN films formed in Examples 21-23 . Like a bar in Fig. (A) and (b) in 15, when the reduction in the peak at 1,400 cm -1, the peak in the XRD (111) was increased, which is a peak at 1,400 cm -1 (111 ) ≪ / RTI > crystal plane.
도 16은 : (a) 예 21 및 24에서 형성된 TiCN 막들의 푸리에 변환 적외 (FT-IR) 스펙트럼들, 및 (b) 예 21 및 24에서 형성된 TiCN 막들의 X-선 회절 (XRD) 분석의 결과들을 나타낸다. 도 16에 있는 (a) 및 (b) 에 나타낸 바처럼, 2,000 cm-1에서의 피크가 감소되었을 때, XRD 에서 (200) 의 피크는 증가되었고, 이는 2,000 cm-1 에서의 피크가 (200) 결정면 상의 원자 배열과 연관되었다는 것을 나타낸다. 일반적으로, (1,400 cm-1 및 2,000 cm-1 에서의) FT-IR 피크들이 감소되고, 막의 결정질은 향상된다.Figure 16 shows the results of X-ray diffraction (XRD) analysis of (a) Fourier transform infrared (FT-IR) spectra of TiCN films formed in Examples 21 and 24 and (b) TiCN films formed in Examples 21 and 24 . Like a bar in Fig. (A) and (b) in 16, when the reduction in the peak at 2,000 cm -1, the peak in the XRD (200) was increased, which is a peak at 2,000 cm -1 (200 ) ≪ / RTI > crystal plane. In general, the FT-IR peaks (at 1,400 cm -1 and 2,000 cm -1 ) are reduced and the crystalline quality of the film is improved.
예 33-40Example 33-40
Ti 함유 막들이, 도 6에 예시된 시퀀스 및 도 1에 예시된 장치를 사용하여 표 8 및 이하의 표 19에 나타낸 조건들하에서 패턴들 (종횡비: 2:1) 을 갖는 기판들 상에 성막되었다.Ti containing films were deposited on substrates having patterns (aspect ratio: 2: 1) under the conditions shown in Table 8 and Table 19 below using the sequence illustrated in FIG. 6 and the apparatus illustrated in FIG. 1 .
이렇게 획득된 막들이 평가되었고, 그 결과들은 도 17에 나타나 있다. 도 17 은 예 33 내지 36에서 막 응력과 수소 흐름 사이의 관계를 나타내는 그래프와, 예 37 내지 40에서 막 응력과 RF 전력 사이의 관계를 나타내는 그래프를 도시한다. 도 17에 나타낸 바처럼, 막 응력은 수소 흐름에 의해 제어되었고, 수소 흐름이 증가되었을 때, 막 응력은 인장성이 되었다 (예 35 및 36). 또한, RF 전력이 증가되었을 때, 막 응력이 압축성이 되었다 (예 40). 제어 파라미터들과 조합하여 수소 흐름 및 RF 전력을 사용함으로써, 막 응력이 약 -2,500 MPa 과 약 +1,000 MPa 사이에서 조정될 수 있다.The thus obtained films were evaluated, and the results are shown in Fig. Figure 17 shows a graph showing the relationship between membrane stress and hydrogen flow in Examples 33-36 and a graph showing the relationship between membrane stress and RF power in Examples 37-40. As shown in Fig. 17, the membrane stress was controlled by the hydrogen flow, and when the hydrogen flow was increased, the membrane stress became tensile (Examples 35 and 36). Also, when the RF power was increased, the membrane stress became compressive (Example 40). By using hydrogen flow and RF power in combination with control parameters, the membrane stress can be adjusted between about -2,500 MPa and about +1,000 MPa.
예 41-44Example 41-44
Ti 함유 막들이, 도 6에 예시된 시퀀스 및 도 1에 예시된 장치를 사용하여 표 8 및 이하의 표 20에 나타낸 조건들하에서 패턴들 (종횡비: 2:1) 을 갖는 기판들 상에 성막되었다.Ti containing films were deposited on substrates having patterns (aspect ratio: 2: 1) under the conditions shown in Table 8 and Table 20 below using the sequence illustrated in FIG. 6 and the apparatus illustrated in FIG. 1 .
이렇게 획득된 막들이 평가되었고, 그 결과들은 표 21에 나타나 있다.The membranes thus obtained were evaluated, and the results are shown in Table 21.
예 41 내지 44에서, TDEAT 가 TDMAT 대신에 사용되었다. 표 21에 나타낸 바처럼, TDEAT 으로부터 도출된 막들에 대한 RF 전력의 효과는 TDMAT 으로부터 도출된 막들에 대한 그것과는 현저히 상이했다. 질소가 사용되었을 때 (예 41), RF 전력이 더 낮았을 때, 탄소 함량이 더 낮은 반면, 수소가 사용되거나 포함되었을 때 (예 42 및 43), RF 전력이 더 낮았을 때, 탄소 함량이 더 높았다. 산소가 사용되었을 때 (예 44), RF 전력은 탄소 함량에 영향을 미치지 않았다. 예 41 내지 44에서, 각 막의 스텝 커버리지는 약 100% 였고, 막 응력은 약 -5,000 MPa 과 +2,000 MPa 사이에서 변화되었고, 또한, 각 막은 습식 식각에 대해 높은 저항을 나타냈다. 예 41 내지 44에서, 막 응력은 400 W 과 600 W 사이의 RF 전력에서 극적으로 변화했고, 이는 결정질 상태가 RF 전력의 함수로서 변화했음을 나타낸다.In Examples 41 to 44, TDEAT was used instead of TDMAT. As shown in Table 21, the effect of RF power on the films derived from TDEAT was significantly different from that for films derived from TDMAT. When nitrogen is used (Example 41), when the RF power is lower, the carbon content is lower, while when the hydrogen is used or included (Examples 42 and 43), when the RF power is lower, Higher. When oxygen was used (Example 44), RF power did not affect the carbon content. In Examples 41 to 44, the step coverage of each film was about 100%, the film stress was changed between about -5,000 MPa and +2,000 MPa, and each film exhibited a high resistance to wet etching. In Examples 41 to 44, the film stress varied dramatically at RF power between 400 W and 600 W, indicating that the crystalline state changed as a function of RF power.
본 발명은 위의 언급된 실시형태들 및 다음을 포함하는 다른 다양한 실시형태들을 포함한다: The present invention includes other various embodiments including the above-mentioned embodiments and the following:
1) TDMAT 또는 TDEAT 를 사용하여 ALD 에 의해 Ti 함유 막을 형성하는 방법에 있어서, 그 방법은, 성막 온도가 50℃ 내지 250℃ (예를 들어, 150℃ 미만) 의 범위에 있고, 오로지 반응물 가스를 변경하는 것에 의해서, 95% 이상의 스텝 커버리지를 갖는 TiO, TiON, TiN, TiCN, 및 TiOCN 막들로부터 선택된 다양한 막들이 기판 상에 성막될 수 있는 것을 특징으로 한다. 특히, 그 방법은, TiN 막이 수소 함유 반응물 그리고 전구체 자체에 포함된 질소를 사용하여, 암모니아 및 질소 등의 질소 함유 반응물 없이, 성막될 수 있는 것을 특징으로 한다. 그 방법은 또한, 인장 응력을 갖는 TiN 막이, 막 응력을 제어하는 목적을 위해 RF 전력 제어 및 시트 저항 제어와 조합하여 반응물 가스로서 수소를 사용하여 성막될 수 있는 것을 특징으로 한다.1) A method of forming a Ti-containing film by ALD using TDMAT or TDEAT, the method being characterized in that the film formation temperature is in the range of 50 to 250 캜 (e.g., less than 150 캜) The various films selected from TiO2, TiON, TiN, TiCN, and TiOCN films having a step coverage of 95% or more can be deposited on the substrate. In particular, the method is characterized in that the TiN film can be deposited without nitrogen-containing reactants such as ammonia and nitrogen, using the hydrogen-containing reactant and the nitrogen contained in the precursor itself. The method is also characterized in that a TiN film with tensile stress can be deposited using hydrogen as the reactant gas in combination with RF power control and sheet resistance control for the purpose of controlling the film stress.
2) 1) 에 따른 방법은, TiCN 막이 반응물로서 질소 또는 수소와 조합한 질소일 때 성막되는 것을 특징으로 한다.2) The method according to 1) is characterized in that a film is formed when the TiCN film is nitrogen combined with nitrogen or hydrogen as a reactant.
3) 1) 에 따른 방법에서, TiON 막 및 TiOCN 막이 각각 TiN 및 TiCN 에 의해 주로 구성되는 막들에 산소를 첨가하는 것에 의해 성막될 수 있고, 여기서 라미네이트 구조는 TiO 층 및 TiN 또는 TiCN 층을 교번하여 성막하는 것에 의해 형성된다. 특히, 그 방법은, TiON 막이 형성될 때, NF3를 사용한 건식 식각 레이트, 불화 수소를 사용한 습식 식각 레이트, 및 시트 저항이 제어될 수 있는 것을 특징으로 한다.3) In the process according to 1), the TiON film and the TiOCN film can be deposited by adding oxygen to the films consisting mainly of TiN and TiCN, respectively, wherein the laminate structure alternates the
4) 1) 에 따른 방법은 TiO 막이 산소 뿐만 아니라 TDMAT 또는 TDEAT 를 사용하여 성막될 수 있는 것을 특징으로 한다.4) The method according to 1) is characterized in that the
5) 1)에 따른 방법에서, 반응물 가스는 TiO, TiON, TiN, TiCN, 또는 TiOCN 막을 형성하기 위하여 He, Ar, H2, N2, O2, N2O, 및 H2O 로 이루어지는 군으로부터 선택된 하나의 가스 또는 혼합된 가스이고, 여기에서 He의 유량은 0 내지 8000 sccm이고, Ar의 유량은 0 내지 8000 sccm이고, H2 의 유량은 0 내지 5000 sccm이고, N2 의 유량은 0 내지 500 sccm이고, O2 의 유량은 0 내지 5000 sccm이고, N2O 의 유량은 0 내지 5000 sccm이고, H2O 의 유량은 0 내지 5000 sccm이다.5) In the process according to 1), the reactant gas is selected from the group consisting of He, Ar, H 2 , N 2 , O 2 , N 2 O and H 2 O to form
6) 1)에 따른 방법에서, 성막되는 막의 조성들이 다음과 같이 제어될 수 있다: C: 0 원자% 내지 25 원자%; Ti: 10 원자% 내지 40 원자%; N: 0 원자% 내지 50 원자%; O: 0 원자% 내지 70 원자%; H: 3 원자% 내지 25 원자%.6) In the method according to 1), the compositions of the film to be deposited can be controlled as follows: C: 0 atom% to 25 atom%; Ti: 10 atom% to 40 atom%; N: 0 atom% to 50 atom%; O: 0 atom% to 70 atom%; H: 3 atom% to 25 atom%.
7) 1) 에 따른 방법은, 막 응력이 다음 중 적어도 어느 하나를 변경함으로써 제어될 수 있다: 처리 온도, 반응물 가스로서 사용되는 H2 의 유량, 및 RF 전력.7) The method according to 1) can be controlled by changing at least one of the following: the processing temperature, the flow rate of H 2 used as the reactant gas, and the RF power.
8) 7) 에 따른 방법에서, 막 응력이 -5,000 MPa 내지 +1,500 MPa의 범위에서 제어될 수 있다.8) In the method according to 7), the film stress can be controlled in the range of -5,000 MPa to +1,500 MPa.
9) 7)에 따른 방법에서, 기판 온도가 70℃ 내지 250℃ 이고, H2 의 유량이 50 sccm 내지 2,000 sccm이고, RF 전력이 150 W 내지 500 W인 조건들하에서 인장 응력이 획득될 수 있다.9) In the method according to 7), tensile stress can be obtained under the conditions that the substrate temperature is 70 ° C. to 250 ° C., the flow rate of H 2 is 50 sccm to 2,000 sccm, and the RF power is 150 W to 500 W .
10) 1) 에 따른 방법에서, 시트 저항이 10Ω/sq. 내지 5,000Ω/sq.의 범위에서 제어될 수 있다.10) The method according to 1), wherein the sheet resistance is 10? / Sq. To 5,000 OMEGA / sq. ≪ / RTI >
11) 3) 에 따른 방법에서, TiO 및 TiN 또는 TiCN 의 각 층의 두께는 0.06 nm 내지 10 nm의 범위에 있다.11) In the method according to 3), the thickness of each layer of
12) 3) 에 따른 방법에서, TiO 층들의 수 대 TiN 또는 TiCN 층들의 수의 비는 예를 들어 두께가 20 nm 인 라미네이트에 대해 1:333 내지 333:1의 범위에 있다.12) In the method according to 3), the ratio of the number of
13) 3) 에 따른 방법은 전체 산소 농도가 TiO 층들의 두께를 감소 또는 증가시키는 것에 의해, 즉, TiN 또는 TiCN 층들의 두께를 상대적으로 증가 또는 감소시키는 것에 의해 제어될 수 있는 것을 특징으로 한다. 위의 방법은 또한, 탄소 농도 및 질소 농도를 제어하는데 사용될 수 있다.13) The method according to 3) is characterized in that the total oxygen concentration can be controlled by reducing or increasing the thickness of the
14) 3) 에 따른 방법에서, TiON 막이 형성되고, NF3 를 사용한 그의 건식 식각 레이트 및 불화 수소를 사용한 습식 식각 레이트는, 라미네이트될 TiO 층들 및 TiN 층들의 수를 변경함으로써 제어될 수 있다.14) In the method according to 3), a TiON film is formed, and its dry etching rate using NF 3 and the wet etching rate using hydrogen fluoride can be controlled by changing the number of
15) 14) 에 따른 방법에서, NF3를 사용한 건식 식각 레이트는 TiO 단일 막의 그것의 0.03 배 내지 1 배로 제어될 수 있고, 라미네이트를 구성하는 층들의 수가 증가할 때, 건식 식각에 대한 저항이 향상, 즉, 증가된다.15) In the method according to 14), the dry etching rate using NF 3 can be controlled to 0.03 to 1 times that of the
16) 14) 에 따른 방법에서, 불화 수소를 사용한 습식 식각 레이트는 TiO 단일 막의 그것의 1 배 내지 10 배로 제어될 수 있고, 라미네이트를 구성하는 층들의 수가 증가할 때, 습식 식각에 대한 저항이 저하, 즉, 감소된다.16) In the method according to 14), the wet etch rate using hydrogen fluoride can be controlled to be 1 to 10 times that of the
17) 1) 에 따른 방법은, 비정질 TiO 막이, 용이하게 산화되는 Ti의 특성에 기인하여 PEALD 에 의해서 뿐만 아니라 열적 ALD 에 의해서도 형성될 수 있는 것을 특징으로 한다.17) The method according to 1) is characterized in that the
18) 1)에 따른 방법은 TiO 막을 형성한 후에 400℃내지 1,000℃의 온도에서 열적 어닐링을 수행하는 것에 의해, 아나타제 타입 TiO2 결정들, 루틸 타입 TiO2 결정들, 또는 브루카이트 타입 TiO2 결정들이 어닐링 온도에 따라 형성될 수 있는 것을 특징으로 한다.18) 1) a method of the by performing a thermal annealing at a temperature of 400 ℃ to 1,000 ℃ after forming film TiO, the anatase type TiO 2 crystal, rutile-type TiO 2 crystal according, or brookite-type TiO 2 crystals Can be formed according to the annealing temperature.
19) 18) 에 따른 방법은 아나타제 타입 TiO2 결정들 또는 루틸 타입 TiO2 결정들이 광촉매 활성을 나타내고, 또한 아나타제 타입 TiO2 결정들이 초친수성을 나타내는 것을 특징으로 한다.19) The method according to 18) is characterized in that anatase type TiO 2 crystals or rutile type TiO 2 crystals exhibit photocatalytic activity, and anatase type TiO 2 crystals exhibit superhydrophilic properties.
20) 1) 에 따른 방법에서, RF 전력이 10 W 내지 2,000 W의 범위에 있다.20) In the method according to 1), the RF power is in the range of 10 W to 2,000 W.
21) 1) 에 따른 방법은 막의 스텝 커버리지가 95% 이상인 것을 특징으로 한다.21) The method according to 1) is characterized in that the step coverage of the film is 95% or more.
22) 1) 에 따른 방법은 실리콘 기판을 유지하는 서셉터의 온도가 0℃ 내지 600℃의 범위에 있고, 장치에 설치된 플라즈마 생성기는 1 MHz 과 60 MHz 사이의 임의의 주파수를 갖는 것을 특징으로 한다.22) The method according to 1), characterized in that the temperature of the susceptor holding the silicon substrate is in the range of 0 ° C. to 600 ° C., and the plasma generator installed in the apparatus has an arbitrary frequency between 1 MHz and 60 MHz .
당업자는, 본 발명의 사상으로부터 이탈함이 없이 수많은 그리고 다양한 변경들이 이루어질 수 있다는 것을 이해할 것이다. 그러므로, 본 발명의 형태들은 단지 예시적이고 본 발명의 범위를 제한하도록 의도된 것이 아니라는 것이 분명히 이해되야 한다. It will be understood by those skilled in the art that numerous and various modifications may be made without departing from the spirit of the invention. It is therefore to be clearly understood that the forms of the invention are illustrative only and are not intended to limit the scope of the invention.
Claims (18)
(i) 기판이 배치되는 반응 공간에 펄스로 TDMAT 및/또는 TDEAT 를 도입하는 단계;
(ii) 상기 반응 공간에 NH3 무함유 반응물 가스를 연속적으로 도입하는 단계;
(iii) 상기 반응 공간에 펄스로 RF 전력을 인가하는 단계로서, TDMAT 및/또는 TDEAT 의 펄스 그리고 RF 전력의 펄스는 오버랩되지 않는, 상기 인가하는 단계; 및
(iv) 상기 기판 상에 Ti 함유 막을 성막하기 위하여 (i) 내지 (iii) 단계들을 반복하는 단계를 포함하는, Ti 함유 막을 형성하는 방법.A method of forming a Ti-containing film on a substrate by plasma enhanced atomic layer deposition (PEALD) using tetrakis (dimethylamino) titanium (TDMAT) or tetrakis (diethylamino) titanium (TDEAT)
(i) introducing TDMAT and / or TDEAT into the reaction space in which the substrate is placed in a pulse;
(ii) continuously introducing an NH 3 -containing reactant gas into the reaction space;
(iii) applying RF power in pulses to the reaction space, wherein pulses of TDMAT and / or TDEAT and pulses of RF power do not overlap; And
(iv) repeating steps (i) to (iii) to form a Ti-containing film on the substrate.
상기 NH3 무함유 반응물 가스는 H2 및/또는 N2인, Ti 함유 막을 형성하는 방법.The method according to claim 1,
Wherein the NH 3 -free reactant gas is H 2 and / or N 2 .
상기 NH3 무함유 반응물 가스는 질소를 함유하지 않거나 또는 산소를 함유하지 않는, Ti 함유 막을 형성하는 방법.The method according to claim 1,
The NH 3 reagent gas-free or containing no oxygen or not contain nitrogen, a method of forming a film containing Ti.
상기 NH3 무함유 반응물 가스는 산소를 포함하는, Ti 함유 막을 형성하는 방법.The method according to claim 1,
Wherein the NH 3 -containing reactant gas comprises oxygen.
상기 NH3 무함유 반응물 가스가 H2 및 희가스로 이루어짐으로써, (iv) 단계에서 상기 Ti 함유 막으로서 TiN 결정질 막을 성막하는, Ti 함유 막을 형성하는 방법.3. The method of claim 2,
Wherein the NH 3 -containing reactant gas is composed of H 2 and a rare gas, thereby forming a Ti-containing crystalline film as the Ti-containing film in the step (iv).
상기 NH3 무함유 반응물 가스가 H2, N2 및 희가스로 이루어짐으로써, (iv) 단계에서 상기 Ti 함유 막으로서 TiCN 비정질 막을 성막하는, Ti 함유 막을 형성하는 방법.3. The method of claim 2,
Wherein the Ti-containing amorphous film is formed as the Ti-containing film in the step (iv), wherein the NH 3 -containing reactant gas is composed of H 2 , N 2 and a rare gas.
상기 Ti 함유 막은 막 응력이 -2,500 MPa 내지 800 MPa 인, Ti 함유 막을 형성하는 방법.The method according to claim 1,
Wherein the Ti-containing film has a film stress of -2,500 MPa to 800 MPa.
(ii) 단계에서 상기 반응물 가스로서 사용된 H2 의 참조 유량 (reference flow rate), (iii) 단계에서 사용된 참조 RF 전력, 및 (i) 내지 (iii) 전체에 걸친 참조 성막 온도를 포함하는 성막 조건들하에서 (i) 내지 (iv) 단계들에 의해 성막되는 TiN 결정질 막의 막 응력보다 더 큰, 상기 Ti 함유 막을 위한 타겟 막 응력을 설정하는 단계; 및
(ii) 단계에서 상기 반응물 가스로서 사용되는 H2 의 유량, (iii) 단계에서 사용되는 RF 전력, 및 (i) 내지 (iii) 단계 전체에 걸친 성막 온도를 설정하는 단계로서, 상기 H2 의 유량, 상기 RF 전력 및 상기 성막 온도 중 하나 이상만이 상기 막 응력을 변경하기 위한 제어 파라미터로서 사용되고, 상기 H2 의 참조 유량, 상기 참조 RF 전력, 및 상기 참조 성막 온도와는 상이한, 상기 설정하는 단계,
다음으로 상기 Ti 함유 막을 성막하기 위해 (i) 내지 (iv) 단계들을 수행하는 단계를 더 포함하는, Ti 함유 막을 형성하는 방법.The method according to claim 1,
the reference flow rate of H 2 used as the reactant gas in step (ii), the reference RF power used in step (iii), and the reference deposition temperature throughout (i) to (iii) Setting a target film stress for the Ti-containing film that is greater than the film stress of the TiN crystalline film deposited by the steps (i) to (iv) under film-forming conditions; And
(ii) a step of setting the film forming temperature throughout the RF power, and (i) - (iii) steps used in the flow rate, (iii) Step of H 2 is used as the reagent gas in the step of the H 2 Wherein at least one of the flow rate, the RF power, and the film forming temperature is used as a control parameter for changing the film stress, and the reference flow rate of H 2 , the reference RF power, and the reference film forming temperature are different from each other ,
And then performing steps (i) to (iv) to form the Ti-containing film.
상기 Ti 함유 막은 인장 막 응력을 갖는, Ti 함유 막을 형성하는 방법.9. The method of claim 8,
Wherein the Ti-containing film has tensile film stress.
설정된 상기 H2 의 유량은 상기 TiN 결정질 막에 사용된 상기 H2 의 참조 유량보다 더 작은, Ti 함유 막을 형성하는 방법.10. The method of claim 9,
The flow rate of the H 2 is set how smaller, a film containing Ti than the reference flow rate of the H 2 used in the TiN crystalline film.
설정된 상기 RF 전력은 상기 TiN 결정질 막에 사용된 상기 참조 RF 전력보다 더 작은, Ti 함유 막을 형성하는 방법.10. The method of claim 9,
Wherein the set RF power is less than the reference RF power used in the TiN crystalline film.
설정된 상기 성막 온도는 상기 TiN 결정질 막에 사용된 상기 참조 성막 온도보다 더 높은, Ti 함유 막을 형성하는 방법.10. The method of claim 9,
Wherein the set film forming temperature is higher than the reference film forming temperature used in the TiN crystalline film.
상기 Ti 함유 막은 약 4% 내지 약 9% 탄소를 함유하는, Ti 함유 막을 형성하는 방법.10. The method of claim 9,
Wherein the Ti containing film contains about 4% to about 9% carbon.
상기 Ti 함유 막은 푸리에 변환 적외 분광 (FT-IR) 그래프에서 2,000 cm-1 에서 피크를 나타내고 1,400 cm-1 에서 실질적으로 피크들을 나타내지 않는, Ti 함유 막을 형성하는 방법.10. The method of claim 9,
Wherein the Ti-containing film exhibits a peak at 2,000 cm < -1 > in a Fourier Transform Infrared Spectroscopy (FT-IR) graph and does not substantially exhibit peaks at 1,400 cm <" 1 & gt ;.
상기 NH3 무함유 반응물 가스는 산소를 함유하지 않는 반응물 가스 그리고 산소를 함유하는 반응물 가스로 구성되고, (iv) 단계에서, (i) 내지 (iii) 단계들이 반복될 때, NH3 무함유 산소 무함유 반응물 가스 및 NH3 무함유 산소 함유 가스가 설정된 인터벌에서 교번하여 사용되는, Ti 함유 막을 형성하는 방법.The method according to claim 1,
In the NH 3-free reaction gas is made up of a reaction gas containing a reaction gas and oxygen that does not contain oxygen, (iv) step, (i) - (iii) when the steps are repeated, NH 3-free oxygen Containing gas and NH 3 -free oxygen containing gas are used alternately at set intervals.
상기 NH3 무함유 산소 무함유 반응물 가스가 질소 가스 없이 수소 가스이고, 상기 NH3 무함유 산소 함유 가스가 산소 가스임으로써, 설정된 인터벌에서 교번하여 성막된 TiO 막들과 TiN 막들로 이루어지는 TiON 막을 형성하는, Ti 함유 막을 형성하는 방법.16. The method of claim 15,
And it said NH 3-free oxygen-free reaction gas is hydrogen gas without nitrogen gas, the NH 3-free oxygen-containing gas is oxygen gas being as, alternately at predetermined intervals to form a film TiON made of a film-forming TiO films and TiN films , A Ti-containing film is formed.
상기 NH3 무함유 산소 무함유 반응물 가스가 수소 가스 및 질소 가스이고, 상기 NH3 무함유 산소 함유 가스가 산소 가스임으로써, 설정된 인터벌에서 교번하여 성막된 TiO 막들과 TiCN 막들로 이루어지는 TiOCN 막을 형성하는, Ti 함유 막을 형성하는 방법.16. The method of claim 15,
Wherein the NH 3 -free oxygen-free reactant gas is a hydrogen gas and a nitrogen gas, and the NH 3 -free oxygen containing gas is oxygen gas, thereby forming a TiOCN film composed of TiO 2 films and TiCN films alternately formed at a predetermined interval , A Ti-containing film is formed.
(iv) 단계에서 상기 Ti 함유 막으로서 아나타제 결정을 갖는 TiO 막을 형성하기 위하여 (iv) 단계 후에 산소의 분위기에서 상기 기판 상에 상기 Ti 함유 막을 어닐링하는 단계를 더 포함하는, Ti 함유 막을 형성하는 방법.The method according to claim 1,
further comprising the step of: (iv) annealing the Ti-containing film on the substrate in an atmosphere of oxygen after the step (iv) so as to form a TiO film having anatase crystal as the Ti-containing film in the step (iv) .
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TWI625414B (en) | 2018-06-01 |
US9556516B2 (en) | 2017-01-31 |
TW201527579A (en) | 2015-07-16 |
KR102332870B1 (en) | 2021-11-29 |
JP6472203B2 (en) | 2019-02-20 |
JP2015074831A (en) | 2015-04-20 |
US20150099072A1 (en) | 2015-04-09 |
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